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Difference between revisions of "Linear phenomenological laws"

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{{MitoPedia
|description='''Linear phenomenological laws''' are at the core of the thermodynamics of irreversible processes TIP, considered to apply near equilibrium but more generally in transport processes (e.g. Fick's law). In TIP, linearity is discussed as the dependence of generalized flows on generalized forces, ''I'' = -''L''·''F'', where ''L'' is expected to be constant (as a prerequisite for linearity) and must not be a function of the force ''F'' ([[affinity]]) for [[Onsager 1931 Phys Rev |Onsager reciprocity]] to apply. This paradigm is challenged by the [[ergodynamics |ergodynamic concept]] of fundamentally non-linear isomorphic flow-[[force]] relations and is replaced by the generalized isomorphic flow-[[pressure]] relations. Flows ''I'' [MU·s<sup>-1</sup>] and forces ''F'' [J·MU<sup>-1</sup>] are conjugated pairs, the product of which yields power, ''I''·''F'' = ''P'' [J·s<sup>-1</sup> = W]. Then [[Vector |vectoral]] and [[Discontinuous system |vectorial]] transport processes are inherently non-linear flow-force relationships, with '''''L''''' = '''''u'''''·'''''c''''' in continuous transport processes along a gradient ('''''c''''' is the local concentration), or ''L'' = ''u''·''α'' (''α'' is the [[free activity]] in a discontinuous transport process across a semipermeable membrane) — formally not different from (isomorphic to) [[scalar]] chemical reactions.
|description='''Linear phenomenological laws''' are at the core of the thermodynamics of irreversible processes TIP, considered to apply near equilibrium but more generally in transport processes (e.g. Fick's law). In TIP, linearity is discussed as the dependence of generalized flows ''I'' or fluxes ''J'' on generalized forces, ''J'' = -''L''·''F'', where ''L'' is expected to be constant (as a prerequisite for linearity) and must not be a function of the force ''F'' ([[affinity]]) for [[Onsager 1931 Phys Rev |Onsager reciprocity]] to apply. This paradigm is challenged by the [[ergodynamics |ergodynamic concept]] of fundamentally non-linear isomorphic flux-[[force]] relations and is replaced by the generalized isomorphic flux-[[pressure]] relations. Flows ''I'' [MU·s<sup>-1</sup>] and forces ''F'' [J·MU<sup>-1</sup>] are conjugated pairs, the product of which yields power, ''I''·''F'' = ''P'' [J·s<sup>-1</sup> = W]. Flux 'J' is system-size specific flow, such that volume-specific flux times force yields volume-specific power, ''P''<sub>''V''</sub> = ''J''·''F'' [W·m<sup>-3</sup>]'. Then [[Vector |vectoral]] and [[Discontinuous system |vectorial]] transport processes are inherently non-linear flux-force relationships, with '''''L''''' = '''''u'''''·'''''c''''' in continuous transport processes along a gradient ('''''c''''' is the local concentration), or ''L'' = ''u''·''α'' (''α'' is the [[free activity]] in a discontinuous transport process across a semipermeable membrane) — formally not different from (isomorphic to) [[scalar]] chemical reactions.


|info=[[Gnaiger 2020 BEC MitoPathways]], [[Gnaiger 1989 Energy Transformations]], [[MitoPedia: Ergodynamics]]
|info=[[Gnaiger 2020 BEC MitoPathways]], [[Gnaiger 1989 Energy Transformations]], [[MitoPedia: Ergodynamics]]
}}
}}
__TOC__
__TOC__
  Communicated by [[Gnaiger Erich]] 2022-10-21
  Communicated by [[Gnaiger Erich]] 2022-10-22


== Linear laws in transport processes are not linear flow-force laws ==
== Linear laws in transport processes are not linear flux-force laws ==


:::: In TIP, the linearity between 'generalized flows' and 'generalized forces' is emphasized to apply to transport processes:
:::: In TIP, the linearity between 'generalized flux' and 'generalized force' is emphasized to apply to transport processes:


::::* 'In contrast to the simple behavior of transport processes, the linear relations between rates and affinities are not always sufficient and in many cases it is necessary to take into account non-linear relations like (5.14).' - (p. 59 in [[Prigogine 1967 Interscience]])
::::* 'In contrast to the simple behavior of transport processes, the linear relations between rates and affinities are not always sufficient and in many cases it is necessary to take into account non-linear relations like (5.14).' - (p. 59 in [[Prigogine 1967 Interscience]])
::::* 'Even in the validity range of the Gibbs formula the relations between chemical rates and affinities may be non-linear (see, i.e., (5.14)). This is in contrast with transport processes where we restrict ourselves to linear laws with respect to the forces. - (p. 94 in [[Prigogine 1967 Interscience]])
::::* 'Even in the validity range of the Gibbs formula the relations between chemical rates and affinities may be non-linear (see, i.e., (5.14)). This is in contrast with transport processes where we restrict ourselves to linear laws with respect to the forces. - (p. 94 in [[Prigogine 1967 Interscience]])
   
   
== Flow-force problems and flow-pressure solutions ==
== Flux-force problems and flux-pressure solutions ==
::::# 'Rates' or generalized [[flux]]es (p. 40 in [[Prigogine 1967 Interscience]]) must be distinguished from [[flow]]s.
::::# Generalized [[flux]]es (p. 40 in [[Prigogine 1967 Interscience]]) must be distinguished from [[flow]]s. The term 'rate' is ambiguous.
::::# An amazingly vague terminology is used in physical chemistry, where 'natural assumptions' are not expected, since such assumptions can be easily replaced by rigorous isomorphic analyses and are falsified by such anayses. 'It is quite natural to assume, at least close to equilibrium, that we have linear relations between the rates and the [[affinity |affinities]]. Such a scheme automatically includes empirical laws as Fourier's law for heat flow or Fick's law for diffusion.' - (p. 44/45 in [[Prigogine 1967 Interscience]]) [[File:Phenomenological coefficient.png|right|300px]]
::::# An amazingly vague terminology is used in physical chemistry, where 'natural assumptions' are not expected, since such assumptions can be easily replaced by rigorous isomorphic analyses and are falsified by such anayses. 'It is quite natural to assume, at least close to equilibrium, that we have linear relations between the rates and the [[affinity |affinities]]. Such a scheme automatically includes empirical laws as Fourier's law for heat flow or Fick's law for diffusion.' - (p. 44/45 in [[Prigogine 1967 Interscience]]) [[File:Phenomenological coefficient.png|right|300px]]
::::# Fick's law for diffusion is a linear law of the form ''I'' = -''u''·Δ''Π'' for discontinuous transport across a semipermeable membrane. ''I'' [mol·s<sup>-1</sup>] times ''Π'' [Pa = J·m<sup>-3</sup>] does not yield power ''P'' [W = J·s<sup>-1</sup>]. Fick's law, therefore, must not be considered as a linear phenomenological flow-force law, but instead a linear flow-pressure law, where the diffusion coefficient is ''D'' = ''u''·''RT'' and ''Π'' = ''RT''·Δ''c''. This yields the more familiar form of Fick's law as ''I'' = -''D''·Δ''c'' = -''u''·''RT''·Δ''c''. The [[free activity]] ''α'' is pressure divided by force, i.e. pressure ''Π'' = ''RT''·Δ''c'' [J·m<sup>-3</sup>] divided by force ''F'' = ''RT''·Δln''c'' [J·mol<sup>-1</sup>]. Then ''α'' = Δ''c''/Δln''c'' [mol·m<sup>-3</sup>]. From Fick's law in the form ''I'' = -''u''·''α''·''F'' it can be seen that the phenomenological coefficient (thermodynamic conductivity ''L'') combines the term mobility ''u'' related to the molecular details (particle size, membrane permeability) and free activity ''α'', ''L'' = ''u''·''α''. Then correctly ''P'' = ''I''·''F''. In contrast, the ergodynamic pressure concept combines the free activity ''α'' and the force ''F'' which are interdependent, ''Π'' = ''α''·''F''.
::::# From ''J'' = ''L''·''X'' in TIP, it follows that affinities ''X'' are generalized forces, ''X'' = -''F''.
::::# The equation for the [[free activity]] ''α'' has been introduced in the context of the Kedem-Katchalsy equations with the quite misleading term 'logarithmic mean concentration' ([[Kedem 1958 Biochim Biophys Acta]]; [[Caplan 1983 Harvard Univ Press]]; [[Demirel 2004 J Phys Chem B]]). By restricting the view in TIP on (''1'') conditions when the phenomenological coefficient ''L'' is fairly constant and (''2'') linear relations between volume-flow and pressure which is actually a unique flow-force relations (instead of the linear relation between flow of a diffusing amount of substance and pressure, which is not a flow-force relation), the fundamental flow-pressure relation escaped attention ([[Gnaiger 1989 Energy Transformations]]; [[Gnaiger 1992 Funct Ecol]]; [[Gnaiger 1993 Hypoxia]]).  
::::# Fick's law for diffusion is a linear law of the form ''I'' = -''u''·Δ''Π'' for discontinuous transport across a semipermeable membrane. ''I'' [mol·s<sup>-1</sup>] times ''Π'' [Pa = J·m<sup>-3</sup>] does not yield power ''P'' [W = J·s<sup>-1</sup>]. Fick's law, therefore, must not be considered as a linear phenomenological flow-force law, but instead a linear flow-pressure law, where the diffusion coefficient is ''D'' = ''u''·''RT'' and ''Π'' = ''RT''·Δ''c''. This yields the more familiar form of [[Fick 1855 Pogg Ann |Fick's law]] as ''I'' = -''D''·Δ''c'' = -''u''·''RT''·Δ''c''. The [[free activity]] ''α'' is pressure divided by force, i.e. pressure ''Π'' = ''RT''·Δ''c'' [J·m<sup>-3</sup>] divided by force ''F'' = ''RT''·Δln''c'' [J·mol<sup>-1</sup>]. Then ''α'' = Δ''c''/Δln''c'' [mol·m<sup>-3</sup>]. From Fick's law in the form ''I'' = -''u''·''α''·''F'' it can be seen that the phenomenological coefficient (thermodynamic conductivity ''L'') combines the term mobility ''u'' related to the molecular details (particle size, membrane permeability) and free activity ''α'', ''L'' = ''u''·''α''. Then correctly ''P'' = ''I''·''F''. In contrast, the ergodynamic pressure concept combines the free activity ''α'' and the force ''F'' which are interdependent, ''Π'' = ''α''·''F''.
::::# When [[flow]] ''I'' ([[extensive quantity]]) is normalized to obtain [[flux]] ''J'' (size-specific quantity), then a flux-force relation is obtained by application of the same normalization to ''L'' and a flux-pressure relation is obtained by application of the same normalization to ''u''.
::::# The equation for the [[free activity]] ''α'' has been introduced in the context of the Kedem-Katchalsy equations with the quite misleading term 'logarithmic mean concentration' ([[Kedem 1958 Biochim Biophys Acta]]; [[Caplan 1983 Harvard Univ Press]]; [[Demirel 2004 J Phys Chem B]]). By restricting the view in TIP on (''1'') conditions when the phenomenological coefficient ''L'' is fairly constant and (''2'') linear relations between volume-flow and pressure, the fundamental flux-pressure relation escaped attention ([[Gnaiger 1989 Energy Transformations]]; [[Gnaiger 1992 Funct Ecol]]; [[Gnaiger 1993 Hypoxia]]), despite the fundamental treatment in [[Einstein 1905 Ann Physik 549 |Einstein's diffusion equation]]. Volume-flow times pressure is actually a unique flow-force relation, the concept of which goes back to [[Maxwell 1867 Phil Trans Royal Soc London |Maxwell (1867)]]. In contrast, the linear relation between flux of a diffusing amount of substance and pressure is not a flux-force relation.
::::# The symbols for isomorphic force ''F'' and pressure ''Π'' are simplified here in a 'short-hand' style and should be replaced by [[iconic symbols]].
::::# When [[flow]] ''I'' ([[extensive quantity]]) is normalized to obtain [[flux]] ''J'' (size-specific quantity), then a flux-force relation is obtained by application of the same normalization to ''I'' and ''L'' in ''I'' = -''L''·''F''. A flux-pressure relation is obtained by application of the same normalization to ''I'' and ''u''.
::::# Concentrations ''c'' should be replaced by [[activity |activities]] in the definition of chemical potentials and free activity ''α''. It should be noted that many methods do not report concentrations but activities in the first place (e.g. electrochemical sensors such as the [[polarographic oxygen sensor]] or the glass pH electrode).
::::# Symbols (''F'', ''Π'', ''L'') are simplified here in a 'short-hand' style which may entail ambiguity and is avoided by using [[iconic symbols]].


== References ==
== References ==


::::# Caplan SR, Essig A (1983) Bioenergetics and linear nonequilibrium thermodynamics. The steady state. Harvard Univ Press, Cambridge:435 pp.
::::# Caplan SR, Essig A (1983) Bioenergetics and linear nonequilibrium thermodynamics. The steady state. Harvard Univ Press, Cambridge:435 pp. - [[Caplan 1983 Harvard Univ Press |»Bioblast link«]]
::::# Demirel Y, Sandler SI (2004) Nonequilibrium thermodynamics in engineering and science. J Phys Chem B 108:31-43.
::::# Demirel Y, Sandler SI (2004) Nonequilibrium thermodynamics in engineering and science. J Phys Chem B 108:31-43. - [[Demirel 2004 J Phys Chem B |»Bioblast link«]]
::::# Gnaiger E (1989) Mitochondrial respiratory control: energetics, kinetics and efficiency. In: Energy transformations in cells and organisms. Wieser W, Gnaiger E (eds), Thieme, Stuttgart:6-17.  
::::# Einstein A (1905) Über die von der molekularkinetischen Theorie der Wärme geforderte Bewegung von in ruhenden Flüssigkeiten suspendierten Teilchen. Ann Physik 4, XVII:549-60. - [[Einstein 1905 Ann Physik 549 |»Bioblast link«]]
::::# Gnaiger E (1992) Optimum efficiency of energy transformation and the evolution of catabolic pathways. Funct Ecol 6:234-41.  
::::# Fick A (1855) Über Diffusion. Pogg Ann 94:59-86. - [[Fick 1855 Pogg Ann |»Bioblast link«]]
::::# Gnaiger E (1993) Efficiency and power strategies under hypoxia. Is low efficiency at high glycolytic ATP production a paradox? In: Surviving hypoxia: Mechanisms of control and adaptation. Hochachka PW, Lutz PL, Sick T, Rosenthal M, Van den Thillart G (eds) CRC Press, Boca Raton, Ann Arbor, London, Tokyo:77-109.  
::::# Gnaiger E (1989) Mitochondrial respiratory control: energetics, kinetics and efficiency. In: Energy transformations in cells and organisms. Wieser W, Gnaiger E (eds), Thieme, Stuttgart:6-17. - [[Gnaiger 1989 Energy Transformations |»Bioblast link«]]
::::# Gnaiger E (1992) Optimum efficiency of energy transformation and the evolution of catabolic pathways. Funct Ecol 6:234-41. - [[Gnaiger 1992 Funct Ecol |»Bioblast link«]]
::::# Gnaiger E (1993) Efficiency and power strategies under hypoxia. Is low efficiency at high glycolytic ATP production a paradox? In: Surviving hypoxia: Mechanisms of control and adaptation. Hochachka PW, Lutz PL, Sick T, Rosenthal M, Van den Thillart G (eds) CRC Press, Boca Raton, Ann Arbor, London, Tokyo:77-109. - [[Gnaiger 1993 Hypoxia |»Bioblast link«]]
::::# Gnaiger E (2020) Mitochondrial pathways and respiratory control. An introduction to OXPHOS analysis. 5th ed. Bioenerg Commun 2020.2. https://doi.org/10.26124/bec:2020-0002
::::# Gnaiger E (2020) Mitochondrial pathways and respiratory control. An introduction to OXPHOS analysis. 5th ed. Bioenerg Commun 2020.2. https://doi.org/10.26124/bec:2020-0002
::::# Kedem O, Katchalsky A (1958) Thermodynamic analysis of the permeability of biological membranes to non-electrolytes. Biochim Biophys Acta 27:229-46.  
::::# Kedem O, Katchalsky A (1958) Thermodynamic analysis of the permeability of biological membranes to non-electrolytes. Biochim Biophys Acta 27:229-46. - [[Kedem 1958 Biochim Biophys Acta |»Bioblast link«]]
::::# Onsager L (1931) Reciprocal relations in irreversible processes. I. Phys Rev 37:405-26.
::::# Onsager L (1931) Reciprocal relations in irreversible processes. I. Phys Rev 37:405-26. [[Onsager 1931 Phys Rev |»Bioblast link«]]
::::# Prigogine I (1967) Introduction to thermodynamics of irreversible processes. Interscience New York, 3rd ed:147pp.  
::::# Prigogine I (1967) Introduction to thermodynamics of irreversible processes. Interscience New York, 3rd ed:147pp. - [[Prigogine 1967 Interscience |»Bioblast link«]]


{{Template:Force and pressure}}
{{Template:Force and pressure}}

Revision as of 09:14, 22 October 2022


high-resolution terminology - matching measurements at high-resolution


Linear phenomenological laws

Description

Linear phenomenological laws are at the core of the thermodynamics of irreversible processes TIP, considered to apply near equilibrium but more generally in transport processes (e.g. Fick's law). In TIP, linearity is discussed as the dependence of generalized flows I or fluxes J on generalized forces, J = -L·F, where L is expected to be constant (as a prerequisite for linearity) and must not be a function of the force F (affinity) for Onsager reciprocity to apply. This paradigm is challenged by the ergodynamic concept of fundamentally non-linear isomorphic flux-force relations and is replaced by the generalized isomorphic flux-pressure relations. Flows I [MU·s-1] and forces F [J·MU-1] are conjugated pairs, the product of which yields power, I·F = P [J·s-1 = W]. Flux 'J' is system-size specific flow, such that volume-specific flux times force yields volume-specific power, PV = J·F [W·m-3]'. Then vectoral and vectorial transport processes are inherently non-linear flux-force relationships, with L = u·c in continuous transport processes along a gradient (c is the local concentration), or L = u·α (α is the free activity in a discontinuous transport process across a semipermeable membrane) — formally not different from (isomorphic to) scalar chemical reactions.


Reference: Gnaiger 2020 BEC MitoPathways, Gnaiger 1989 Energy Transformations, MitoPedia: Ergodynamics

Communicated by Gnaiger Erich 2022-10-22

Linear laws in transport processes are not linear flux-force laws

In TIP, the linearity between 'generalized flux' and 'generalized force' is emphasized to apply to transport processes:
  • 'In contrast to the simple behavior of transport processes, the linear relations between rates and affinities are not always sufficient and in many cases it is necessary to take into account non-linear relations like (5.14).' - (p. 59 in Prigogine 1967 Interscience)
  • 'Even in the validity range of the Gibbs formula the relations between chemical rates and affinities may be non-linear (see, i.e., (5.14)). This is in contrast with transport processes where we restrict ourselves to linear laws with respect to the forces. - (p. 94 in Prigogine 1967 Interscience)

Flux-force problems and flux-pressure solutions

  1. Generalized fluxes (p. 40 in Prigogine 1967 Interscience) must be distinguished from flows. The term 'rate' is ambiguous.
  2. An amazingly vague terminology is used in physical chemistry, where 'natural assumptions' are not expected, since such assumptions can be easily replaced by rigorous isomorphic analyses and are falsified by such anayses. 'It is quite natural to assume, at least close to equilibrium, that we have linear relations between the rates and the affinities. Such a scheme automatically includes empirical laws as Fourier's law for heat flow or Fick's law for diffusion.' - (p. 44/45 in Prigogine 1967 Interscience)
    Phenomenological coefficient.png
  3. From J = L·X in TIP, it follows that affinities X are generalized forces, X = -F.
  4. Fick's law for diffusion is a linear law of the form I = -u·ΔΠ for discontinuous transport across a semipermeable membrane. I [mol·s-1] times Π [Pa = J·m-3] does not yield power P [W = J·s-1]. Fick's law, therefore, must not be considered as a linear phenomenological flow-force law, but instead a linear flow-pressure law, where the diffusion coefficient is D = u·RT and Π = RT·Δc. This yields the more familiar form of Fick's law as I = -D·Δc = -u·RT·Δc. The free activity α is pressure divided by force, i.e. pressure Π = RT·Δc [J·m-3] divided by force F = RT·Δlnc [J·mol-1]. Then α = Δc/Δlnc [mol·m-3]. From Fick's law in the form I = -u·α·F it can be seen that the phenomenological coefficient (thermodynamic conductivity L) combines the term mobility u related to the molecular details (particle size, membrane permeability) and free activity α, L = u·α. Then correctly P = I·F. In contrast, the ergodynamic pressure concept combines the free activity α and the force F which are interdependent, Π = α·F.
  5. The equation for the free activity α has been introduced in the context of the Kedem-Katchalsy equations with the quite misleading term 'logarithmic mean concentration' (Kedem 1958 Biochim Biophys Acta; Caplan 1983 Harvard Univ Press; Demirel 2004 J Phys Chem B). By restricting the view in TIP on (1) conditions when the phenomenological coefficient L is fairly constant and (2) linear relations between volume-flow and pressure, the fundamental flux-pressure relation escaped attention (Gnaiger 1989 Energy Transformations; Gnaiger 1992 Funct Ecol; Gnaiger 1993 Hypoxia), despite the fundamental treatment in Einstein's diffusion equation. Volume-flow times pressure is actually a unique flow-force relation, the concept of which goes back to Maxwell (1867). In contrast, the linear relation between flux of a diffusing amount of substance and pressure is not a flux-force relation.
  6. When flow I (extensive quantity) is normalized to obtain flux J (size-specific quantity), then a flux-force relation is obtained by application of the same normalization to I and L in I = -L·F. A flux-pressure relation is obtained by application of the same normalization to I and u.
  7. Concentrations c should be replaced by activities in the definition of chemical potentials and free activity α. It should be noted that many methods do not report concentrations but activities in the first place (e.g. electrochemical sensors such as the polarographic oxygen sensor or the glass pH electrode).
  8. Symbols (F, Π, L) are simplified here in a 'short-hand' style which may entail ambiguity and is avoided by using iconic symbols.

References

  1. Caplan SR, Essig A (1983) Bioenergetics and linear nonequilibrium thermodynamics. The steady state. Harvard Univ Press, Cambridge:435 pp. - »Bioblast link«
  2. Demirel Y, Sandler SI (2004) Nonequilibrium thermodynamics in engineering and science. J Phys Chem B 108:31-43. - »Bioblast link«
  3. Einstein A (1905) Über die von der molekularkinetischen Theorie der Wärme geforderte Bewegung von in ruhenden Flüssigkeiten suspendierten Teilchen. Ann Physik 4, XVII:549-60. - »Bioblast link«
  4. Fick A (1855) Über Diffusion. Pogg Ann 94:59-86. - »Bioblast link«
  5. Gnaiger E (1989) Mitochondrial respiratory control: energetics, kinetics and efficiency. In: Energy transformations in cells and organisms. Wieser W, Gnaiger E (eds), Thieme, Stuttgart:6-17. - »Bioblast link«
  6. Gnaiger E (1992) Optimum efficiency of energy transformation and the evolution of catabolic pathways. Funct Ecol 6:234-41. - »Bioblast link«
  7. Gnaiger E (1993) Efficiency and power strategies under hypoxia. Is low efficiency at high glycolytic ATP production a paradox? In: Surviving hypoxia: Mechanisms of control and adaptation. Hochachka PW, Lutz PL, Sick T, Rosenthal M, Van den Thillart G (eds) CRC Press, Boca Raton, Ann Arbor, London, Tokyo:77-109. - »Bioblast link«
  8. Gnaiger E (2020) Mitochondrial pathways and respiratory control. An introduction to OXPHOS analysis. 5th ed. Bioenerg Commun 2020.2. https://doi.org/10.26124/bec:2020-0002
  9. Kedem O, Katchalsky A (1958) Thermodynamic analysis of the permeability of biological membranes to non-electrolytes. Biochim Biophys Acta 27:229-46. - »Bioblast link«
  10. Onsager L (1931) Reciprocal relations in irreversible processes. I. Phys Rev 37:405-26. »Bioblast link«
  11. Prigogine I (1967) Introduction to thermodynamics of irreversible processes. Interscience New York, 3rd ed:147pp. - »Bioblast link«

Force or pressure? - The linear flux-pressure law

Gnaiger 2020 BEC MitoPathways
"For many decades the pressure-force confusion has blinded the most brilliant minds, reinforcing the expectation that Ohm’s linear flux-force law should apply to the hydrogen ion circuit and protonmotive force. .. Physicochemical principles explain the highly non-linear flux-force relation in the dependence of LEAK respiration on the pmF. The explanation is based on an extension of Fick’s law of diffusion and Einstein’s diffusion equation, representing protonmotive pressure ― isomorphic with mechanical pressure, hydrodynamic pressure, gas pressure, and osmotic pressure ― which collectively follow the generalized linear flux-pressure law."
Gnaiger E (2020) Mitochondrial pathways and respiratory control. An introduction to OXPHOS analysis. 5th ed. Bioenerg Commun 2020.2. https://doi.org/10.26124/bec:2020-0002
» pressure = force × free activity


MitoPedia concepts: Ergodynamics