Michael Polanyi

Michael Polanyi, FRS (11 March 1891 – 22 February 1976) was a Hungarian polymath, who made theoretical contribution to physical chemistry, economics, and philosophy. Polanyi was a well known theoretical chemist who contributed to the chemistry field through three main areas of study: adsorption of gases on solids, x-ray structure analysis of the properties of solids, and the rate of chemical reactions. However, Polanyi was active in both theoretical and experimental studies within the Chemistry field. Polanyi obtained a degree in medicine in 1913 as well as a Ph.D. in physical chemistry in 1917 from the University of Budapest. Later in his life, he taught as a chemistry professor at the Kaiser Wilhelm Institute in Berlin as well as the University of Manchester in Manchester, England.

History

Polanyi potential adsorption theory

The Polanyi potential adsorption theory is based on the assumption that the molecules near a surface move according to a potential, similar to that of gravity or electric fields.^[3] This model is applicable in the case of gases at a surface at constant temperature. Gas molecules move closer to that surface when the pressure is higher than the equilibrium vapor pressure. The change in potential relative to the distance from the surface can be calculated using the formula for difference of the chemical potential,

${\displaystyle \mathrm {d} \mu =-S_{\rm {m}}\,\mathrm {d} T+V_{\rm {m}}\,\mathrm {d} p+\mathrm {d} U_{\rm {m}}}$

where ${\displaystyle \mu }$ is the chemical potential, ${\displaystyle S_{\rm {m}}}$ is the molar entropy, ${\displaystyle V_{\rm {m}}}$ is the molar volume, and ${\displaystyle U_{\rm {m}}}$ is the molar internal energy.

At equilibrium, the chemical potential of a gas at a distance ${\displaystyle r}$ from a surface, ${\displaystyle {\mu (r,p_{r})}}$, is equal to the chemical potential of the gas at an infinitely large distance from the surface, ${\displaystyle {\mu (\infty ,p)}}$. As a result, the integration from an infinitely far distance to r distance from the surface leads to

${\displaystyle \int _{\mu (\infty ,p)}^{\mu (r,p_{r})}\mathrm {d} \mu ={\mu (r,P_{r})}-{\mu (\infty ,p)}=0}$

where ${\displaystyle p_{r}}$ is the partial pressure at distance r and ${\displaystyle p}$ is the partial pressure at infinite distance from the surface.

Since the temperature remains constant, the difference in chemical potential formula can be integrated over pressures ${\displaystyle p}$ and ${\displaystyle p_{r}}$

${\displaystyle \int _{p}^{p_{r}}V_{\rm {m}}\,\mathrm {d} P+U_{\rm {m}}(r)-U_{\rm {m}}(\infty )=0}$

By setting the ${\displaystyle U_{\rm {m}}(\infty )=0}$, the equation can be simplified to

${\displaystyle -U_{\rm {m}}(r)=\int _{p}^{p_{r}}V_{\rm {m}}\,\mathrm {d} p}$

Using the ideal gas law, ${\displaystyle pV_{\rm {m}}=RT}$, the following formula is obtained

${\displaystyle -U_{\rm {m}}(r)=\int _{p}^{p_{r}}{\frac {RT}{p}}\mathrm {d} p=RT\ln {\frac {p_{r}}{p}}}$

Since gas condenses into a liquid on a surface when the pressure of the gas exceeds the equilibrium vapor pressure, ${\displaystyle p_{0}}$, we can assume a liquid film forms over the surface of thickness, ${\displaystyle \delta }$. The energy at ${\displaystyle p_{0}}$ is

${\displaystyle U_{\rm {m}}(\delta )=-RT\ln {\frac {p_{0}}{p}}}$

Considering that the partial pressure of the gases relates to the concentration, the adsorption potential, ${\displaystyle \varepsilon _{\rm {s}}}$ can be calculated as

${\displaystyle \varepsilon _{s}=-RT\ln {\frac {c_{\rm {s}}}{c}}}$

where ${\displaystyle c_{\rm {s}}}$ is the saturated concentration of adsorbate and ${\displaystyle c}$ is the equilibrium concentration of the adsorbate.

Theories based on Polanyi adsorption theory

The potential theory underwent many refinements and changes throughout the years since its first report. One major theories of note that was developed using Polanyi's theory was the Dubinin theories, Dubinin–Radushkivech and Dubinin–Astakhov equations.

Using the adsorption potential, the degree of filling of the adsorption space, ${\displaystyle \theta }$, can be calculated as

${\displaystyle \theta =a/a_{0}=\mathrm {e} ^{{({A/E})}^{b}}}$

where ${\displaystyle a}$ is value of adsorption at temperature T and equilibrium pressure p, ${\displaystyle a_{0}}$ is the maximum value of adsorption, and ${\displaystyle E}$ is the characteristic energy of adsorption in kJ/mol, ${\displaystyle A}$ is the loss in Gibbs free energy in adsorption equal to ${\displaystyle \Delta G=-RT\log(p_{0}/p)}$ and ${\displaystyle b}$ is the fitting coefficient.^[4] The Dubinin–Radushkivech equation where ${\displaystyle b}$ is equal to 2 and the optimized Dubinin-Astakhov equation where ${\displaystyle b}$ is fit to experimental data can be simplified to

${\displaystyle \log a=\log a_{0}+0.434\left({\frac {A}{E}}\right)^{b}}$

Other studies have used the Dubinin–Astakhov in a similar form of ${\displaystyle \log q_{\rm {e}}=\log Q^{0}+(\varepsilon _{\rm {sw}}/E)^{b}}$,

where ${\displaystyle q_{\rm {e}}}$ is equilibrium adsorbed concentration of adsorbent in mg/g, ${\displaystyle Q^{0}}$ is maximum adsorbed concentration of adsorbent in mg/g, ${\displaystyle \varepsilon _{\rm {sw}}}$ is the effective adsorption potential, where equal to ${\displaystyle \varepsilon _{\rm {sw}}=-RT\ln(c_{\rm {e}}/c_{\rm {s}})}$, ${\displaystyle c_{\rm {e}}}$ is equilibrium concentration of adsorbent in the solution phase in mg/L, and ${\displaystyle c_{\rm {s}}}$ is the adsorbent solubility in water in mg/L.^[5]

The characteristic energy of adsorption can be related to a characteristic energy of adsorption for a standard vapor on the same surface, ${\displaystyle E_{0}}$, through the use of an affinity coefficient, ${\displaystyle \beta }$

${\displaystyle E=\beta E_{0}}$

The affinity coefficient is a ratio of the properties of the sample and standard vapors

${\displaystyle \beta ={\frac {\alpha }{\alpha _{0}}}}$

where ${\displaystyle \alpha }$ and ${\displaystyle \alpha _{0}}$ are the polarizabilities of the sample and standard vapors, respectively. Many studies have been performed to determine optimal fitting coefficients, ${\displaystyle b}$, and affinity coefficients, ${\displaystyle \beta }$, to best describe the adsorption of gases and vapors onto solids. As a result, the Dubinin–Astakhov equation remains in use in adsorption studies due to the accuracy it can obtain when fitted with experimental results.

Dubinin–Astakhov parameters for vapors and gases

More information , ...

Compound	Activated carbon	${\displaystyle b}$	${\displaystyle \beta E}$, kJ/mol	${\displaystyle \beta }$	Source
Benzene	Carbon molecular sieve	1.78	11.52	1.00	[6]
Acetone	Carbon molecular sieve	2.00	9.774	0.85	[6]
Benzene	CAL AC	2	18.23	1.00	[7]
Acetone	CAL AC	2	13.21	0.72	[7]
Acetone	Carbon molecular sieve	2.8	20.29	0.72	[8]
Benzene	Carbon molecular sieve	3.1	28.87	1.00	[8]
Nitrogen	Carbon molecular sieve	2.6	11.72	0.41	[8]
Oxygen	Carbon molecular sieve	2.3	9.21	0.32	[8]
Hydrogen	Carbon molecular sieve	2.5	5.44	0.19	[8]

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Characterization of carbon nanoparticles

Historically, the theory was used to model nonuniform adsorbates and multi-components solutes. For certain pairs of adsorbates and adsorbents, the mathematical parameters of the Polyani theory can be related to the physicochemical properties of both adsorbents and adsorbates. The theory has been used to model the adsorption of carbon nanotubes and carbon nanoparticles. In the study done by Yang and Xing,^[5] the theory have been shown to better fit the adsorption isotherm than Langmuir, Freundlich, and partition. The experiment studied the adsorption of organic molecules on carbon nanoparticles and carbon nanotubes. According to the Polyani theory the surface defect curvatures of carbon nanoparticles could affect their adsorption. Flat surfaces on the particles will allow more surface atoms to approach adsorbing organic molecules which will increase the potential, leading to stronger interactions. The theory has been beneficial in trying to understand the adsorption mechanisms of organic compounds on carbon nanoparticles and estimating the adsorption capacity and affinity. Using this theory, researchers are hoping to be able to design carbon nanoparticles for specific needs such as using them as sorbents in environmental studies.

Adsorption from different systems

In one of the earlier studies conducted by Manes, M., & Hofer, L. J. E.,^[10] the Polyani theory was used to characterize liquid-phase adsorption isotherms on various concentrations activated carbon using a wide range of organic solvent. The polyani theory was shown to be a good fit for these various systems. Because of the results, the study introduced the possibility of predicting isotherms for similar systems using minimal data. However, the limitation is that the adsorption isotherms for a large variety of solvents can only fit over a limited range. The curve was not able to fit the data at high-capacity range. The study also concluded that there were a few anomalies in the results. The adsorption from carbon tetrachloride, cyclohexane, and carbon disulfide onto activated carbon was not able to fit well to the curve, and remain to be explained. The researchers who conducted the experiment speculate that steric effects of carbon tetrachloride and cyclohexane may have played a role. The study has been done with a variety of systems such as organic liquids from water solutions and organic solids from water solutions.

Competitive adsorption

Since a variety of systems have been investigated, a study was done to investigate the individual adsorption of a mixed solution. This phenomenon is also called competitive adsorption because solutes tend to compete for the same adsorption sites. In the experiment conducted by Rosene and Manes,^[11] the competitive adsorption of glucose, urea, benzoic acid, phthalide, and p-nitrophenol. Using the Polanyi adsorption model, they were able to calculate the relative adsorption of each compound onto the surface of activated carbon.