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Article

The Effect of Temperature on the Surface Energetic Properties of Carbon Fibers Using Inverse Gas Chromatography

1
Faculty of Science and Engineering, Maastricht University, P.O. Box 616, 6200 MD Maastricht, The Netherlands
2
Laboratory of Materials, Catalysis, Environment and Analytical Methods (MCEMA), Faculty of Sciences, Lebanese University, Hadath P.O. Box 6573, Lebanon
Submission received: 28 November 2023 / Revised: 16 December 2023 / Accepted: 20 December 2023 / Published: 26 December 2023
(This article belongs to the Special Issue Synthesis and Application of Nanocomposite Materials)

Abstract

:
This paper constitutes an original and new methodology for the determination of the surface properties of carbon fibers in two forms, namely, oxidized and untreated, using the inverse gas chromatography technique at infinite dilution based on the effect of temperature on the surface area of various organic molecules adsorbed on the carbon fibers. The studied thermal effect showed a large deviation from the classical methods or models relative to the new determination of the surface properties of carbon fibers, such as the dispersive component of their surface energy, the free surface energy, the free specific energy, and the enthalpy and entropy of the adsorption of molecules on the carbon fibers. It was highlighted that the variations in the London dispersive surface energy of the carbon fibers as a function of the temperature satisfied excellent linear variations by showing large deviations between the values of γ s d   ( T ) , calculated using different models, which can reach 300% in the case of the spherical model. All models and chromatographic methods showed that the oxidized carbon fibers gave larger specific free enthalpy of adsorption whatever the adsorbed polar molecules. The obtained specific enthalpy and entropy of the adsorption of the polar solvents led to the determination of the Lewis acid–base constants of the carbon fibers. Different molecular models and chromatographic methods were used to quantify the surface thermodynamic properties of the carbon fibers, and the results were compared with those of the thermal model. The obtained results show that the oxidized carbon fibers gave more specific interaction energy and greater acid–base constants than the untreated carbon fibers, thus highlighting the important role of oxidization in the acid–base of fibers. The determination of the specific acid–base surface energy of the two carbon fibers showed greater values for the oxidized carbon fibers than for the untreated carbon fibers. An important basic character was highlighted for the two studied carbon fibers, which was larger than the acidic character. It was observed that the carbon fibers were 1.4 times more acidic and 2.4 times more basic. The amphoteric character of the oxidized fibers was determined, and it was 1.7 times more important than that of the untreated fibers This tendency was confirmed by all molecular models and chromatographic methods. The Lewis acid and base surface energies of the solid surface, γ s + and γ s , as well as the specific acid–base surface energy γ s A B of the carbon fibers at different temperatures were determined. One showed that the specific surface energy γ s A B of the oxidized fibers was 1.5 times larger than that of the untreated fibers, confirming the above results obtained on the strong acid–base interactions of the oxidized carbon fibers with the various polar molecules.

1. Introduction

Carbon fibers exhibit excellent physicochemical and mechanical properties, and they are used as alternatives to conventional metals for various applications, especially for decreasing the weight of conventional products. The technical progress of carbon fibers has led to an enhanced elastic modulus by increasing the size of crystals and arranging them along the fiber axis [1].
Carbon fibers are chemically inert materials and are not influenced by air, humidity, weak acids, alkalis or solvents at ambient temperatures. Nevertheless, they suffer from oxidation at higher temperatures [2]. Carbon fibers are mostly composed of carbon atoms (from 92% to 99% carbon). They are extremely stiff, possess high tensile strength and low weight and exhibit excellent resistance to chemical corrosion. Their low thermal expansion is an excellent advantage in different applications requiring good stability [1]. The science and technology of carbon fiber production has been well developed in the literature [2,3,4,5].
These interesting properties have made carbon fibers very popular in aerospace applications, civil engineering, the military and motorsports, along with other competitive sports. However, they are relatively expensive when compared with similar fibers, such as plastic fibers. The exceptional mechanical properties of carbon fibers are advantageously used in composite applications, where their low weight is an excellent factor in some industrial applications, such as aerospace sectors, the military, turbine blades, construction, lightweight cylinders and pressure vessels, off-shore tethers and drilling risers, medicine, automobiles and sporting goods.
In recent years, the carbon fiber industry has been growing steadily to meet the demand from different industries, such as the aerospace industry (aircraft and space systems), the military, turbine blades, construction (non-structural and structural systems), lightweight cylinders and pressure vessels, off-shore tethers and drilling risers, medicine, automobiles and sporting goods [6,7,8,9,10,11,12]. For the automotive industry, fiber-reinforced polymeric composites offer reduced weight and superior styling. Carbon fibers can find applications in body parts (doors, hoods, deck lids, front end, bumpers, etc.), chassis and suspension systems (e.g., leaf springs), drive shafts and so on [12].
The large specific surface area, controllable chemical compositions, excellent electrical conductivity and rich composite forms of carbon fibers are promising for future applications in energy conversion technologies and new challenges and prospects for fiber materials in electrocatalysis applications [13].
Many authors were previously interested in the characterization of the dispersive and specific interactions of carbon fibers using inverse gas chromatography (IGC) at infinite dilution and, more particularly, by determining the surface physicochemical properties of carbon fibers, such as their dispersive component of surface energy, their free energy of adsorption and their specific enthalpy and entropy of the adsorption of some model organic molecules on the carbon fibers [4,5,12,13,14,15,16]. Other recent studies were devoted to determining the effect of oxidation temperature on some commercial carbon fibers [17] or to optimizing the testing conditions of various carbon fiber bundles [18]. Pala et al. [19] studied the surface energy and acid–base properties of some highly porous activated carbons by using inverse gas chromatography. However, the values of different surface thermodynamic parameters previously obtained by different authors [4,5,12,13,14,15,16] using classic chromatographic methods were recently criticized in the literature [20,21,22,23,24]. The effect of the temperature of organic solvents on the surface properties of carbon fibers has never been studied.
Because of the extreme importance of the physicochemical properties of carbon fibers in many different industrial applications, in this paper, we are interested in the correction of the various surface parameters of carbon fibers in two forms, namely, untreated and oxidized, by taking into account the recent progress in the inverse gas chromatography technique.

2. IGC Methods and Models

2.1. Classical Methods

Many papers have been devoted to the determination of the surface physicochemical properties and the Lewis acid–base parameters of solid surfaces in both powder and fiber forms by using the IGC technique at infinite dilution [25,26,27,28,29,30,31,32,33,34,35,36]. Such studies concentrated on the determination of the dispersive surface energy and the specific energy, and the enthalpy and entropy of the adsorption of n-alkanes and polar molecules on oxides, metals or polymers. To that end, several methods were used. These various methods were based on the linear relations found between the free energy of adsorption G a T or RTln(Vn) (at various values of temperature T) as a function of certain reference thermodynamic parameters, where R is the ideal gas constant, and Vn the net retention volume of the injected probes into a chromatographic column containing the solid substrate. In the IGC technique, polar or non-polar organic solvents were used. The used non-polar molecules were the n-alkanes (from n-pentane C5 to n-decane C10) describing the dispersive properties of the solid surfaces. In general, polar solvents comprise the following: acetone, ethyl acetate, ethyl oxide, toluene, benzene, acetonitrile, ethanol, propanol, carbon tetrachloride, chloroform and dichloromethane.
Different reference thermodynamic parameters were used:
  • The boiling point T B . P . of the solvents [25];
  • The vapor pressure P 0 of the probes at a fixed temperature [26,27];
  • The dispersive component γ l d of the surface energy of the solvent [14];
  • The deformation polarizability α 0 [28];
  • The standard enthalpy of the vaporization H v a p . 0 (supposed constant) of the organic molecules [29,30];
  • The topological index χ T of the solvents [31,32].
New molecular models and IGC methods [20,21,22] were proposed based on the linear dependency of R T l n ( V n ) obtained from IGC measurements, with respect to any of the thermodynamic parameters X j of organic molecules.
By varying the temperature of the column, one can obtain the values of the specific free energy G a s p ( T ) of polar molecules adsorbed on solid surfaces by calculating the distance relating the representative point of R T l n ( V n ) of a polar molecule to its hypothetic point located on the n-alkane straight line. The specific enthalpy H a s p and entropy S a s p of the adsorbed polar molecule are then deduced from relation (1):
G a s p T = H a s p T   S a s p
And, consequently, one obtains the acid–base constants KA and KD of the solids from the following relation [26,27]:
H S p A N = D N A N K A + K D
where AN and DN respectively represent the electron donor and acceptor numbers of the polar molecule given by Gutmann [33] and corrected by Fowkes.
However, we can determine the dispersive component γ s d of the surface energy of a solid surface by using the method of Dorris–Gray [34] based on Fowkes’s relation [35]. The obtained relation giving γ s d ( T ) is the following:
γ s d = R T l n V n C n + 1 H 2 ( n + 2 ) V n C n H 2 ( n + 1 ) 2 4 N 2 a C H 2 2 γ C H 2
where C n H 2 ( n + 1 ) and C n + 1 H 2 ( n + 2 ) are two consecutive n-alkanes; a C H 2 is the surface area of the methylene group, with a C H 2 = 6   Å independent of the temperature; and the surface energy γ C H 2 is equal to   γ C H 2 i n   m J / m 2 = 52.603 0.058 T   T   i n   K .
Another equivalent method was proposed in the literature [14], and it allows for the determination of γ s d of solid surfaces by using the following relation:
R T l n ( V n ) = 2 N a γ l d γ s d 1 / 2 + α ( T )
where a is the surface area of an adsorbed molecule (previously supposed constant), N is the Avogadro number, and α ( T ) is a constant depending only on the temperature and the solid substrate.

2.2. Recent Progress

2.2.1. Molecular Models

The values of the dispersive surface energy γ s d of solid substrates proposed by relations (3) and (4) were obtained by supposing that the surface areas of the methylene group and the organic molecules are constant independent of the temperature. It was also supposed that γ l d is constant. In previous works [24], one proposed different molecular models allowing the determination of the surface areas of molecules:
  • Kiselev results;
  • Two-dimensional Van der Waals (VDW) equation;
  • Two-dimensional Redlich–Kwong (R-K) equation;
  • Geometric model based on the real form of molecules;
  • Cylindrical model based on cylindrical form of molecules;
  • Spherical model based on spherical form of molecules.
Table S1 gives the surface areas of n-alkanes for the different molecular models. Furthermore, the dispersive component of the surface tension of the solvents depended on the temperature.

2.2.2. Hamieh Thermal Model

In recent studies, one showed that the surface area of molecules extremely depends on the temperature [20,21,22]. Consequently, the new results will correct the values of γ s d , G a s p and the Lewis acid–base constants. Indeed, new expressions for the surface area a T of organic molecules and n-alkanes were proposed as a function of the temperature. It was also determined that the surface area of methylene group a C H 2 T depends on the temperature [20,21,22]. One also showed that γ l d linearly depends on the temperature.
These new findings allowed us to determine the surface thermodynamic properties of carbon fibers by using all classical IGC methods and the molecular models of the surface areas of molecules. The values of the surface parameters obtained using the classical methods were corrected by our new thermal model taking into account the variations in the surface areas and γ l d ( T ) of organic molecules as a function of the temperature. In Table S2, we give the expressions of γ l d ( T ) of n-alkanes.

3. Experimental Section

3.1. Materials and Solvents

All used n-alkanes (hexane, heptane, octane, nonane) and polar solvents, of highly pure grade (99%), were purchased from Fisher Scientific (Lebanon, Beirut). The used polar molecules were, in Lewis terms, acidic, such as carbon tetrachloride (CCl4), chloroform (CHCl3) and dichloromethane (CH2Cl2); amphoteric, such as acetone; basic, such as ethyl acetate, diethyl ether and tetrahydrofuran (THF); and weak amphoteric, such as benzene. Two carbon fibers were analyzed: untreated fibers and oxidized fibers. The corrected acceptor number and normalized donor number of the electrons of the polar solvents are given in Table S3.

3.2. GC Conditions

Experimental measurements were performed on a commercial Focus GC gas chromatograph equipped with a flame ionization detector. The carbon fibers were filled into a stainless-steel column with a 2 mm inner diameter and a length of 20 cm. The temperature range varied from 40 °C to 100 °C. The different experimental conditions are typically the same as those given in previous published papers [20,21,22]. The column was packed with 1 g of carbon fibers with a diameter of 10 mm and a length of 50 cm. The standard deviation of the obtained retention time, tR, was less than 1% in all measurements.

3.3. Results

3.3.1. Dispersive Component of Surface Energy of Carbon Fibers

All previous various molecular models and the Dorris–Gray method were used to determine the dispersive component of the surface energy of the carbon fibers (untreated and oxidized). The results were compared to those obtained using the thermal model [20,21,22] (Figure 1). The variations in γ s d   ( T ) of the carbon fibers as a function of the temperature satisfied excellent linear variations. Figure 1 shows large deviations between the values of γ s d   ( T ) calculated using the different models, which can reach 300% in the case of the spherical model. The application of the Dorris–Gray relation gave large values of γ s d   ( T ) in the case of the thermal model. The most accurate results were obtained using the thermal model [20,21,22]. One observed that the results of the thermal model (by using the results on PE) were very close to those of the cylindrical, Kiselev, Dorris–Gray and VDW models, whereas the average values gave similar results to those of the thermal model (on PTFE). Furthermore, a comparison between the dispersive surface energy of the carbon fiber types showed small differences not exceeding 10% in all used molecular models. One found a weaker decrease in γ s d   ( T ) in the case of the oxidized carbon fiber.
Table 1 shows the various equations of γ s d ( T ) relative to the carbon fibers for all used molecular models. Other new surface parameters were deduced and are presented below:
  • The dispersive surface entropy ε s d , given by ε s d = d γ s d / d T
  • The extrapolated values γ s d ( T = 0   K   ) at 0 K;
  • The maximum temperature T M a x defined by T M a x = γ s d ( T = 0   K ) ε s d .
Table 1 shows that the dispersive surface entropy ε s d representing the slope of the straight line of γ s d T negatively increased in the case of the oxidized carbon fibers by about 30% for all molecular models, proving a stronger decrease in γ s d ( T ) of the treated fibers when the temperature increased but characterized by a smaller maximum temperature T M a x .
By applying the new thermal model, one confirmed a difference between the values of the maximum temperature T M a x of the two carbon fibers (a) and (b) approaching 500 K.

3.3.2. Specific Variables of Adsorption and Lewis Acid–Base Constants

The experimental chromatographic results allowed for the determination of the retention time and retention volume of the n-alkanes and polar solvents adsorbed on the two carbon fibers (a) and (b). Tables S4 and S5 show the values of RTln(Vn) of the different solvents as a function of the temperature, and the evolution is represented in Figures S1 and S2. The results shown in Tables S4 and S5 and Figures S1 and S2 clearly show that the oxidized carbon fibers (b) gave greater values of RTln(Vn) and therefore exhibited larger interactions than the untreated carbon fibers (a). One also observed an excellent linearity of the curves representing RTln(Vn) versus the temperature for the different n-alkanes and polar solvents.
In order to quantify the specific interactions of the two fibers, one determined the values of the specific free energy ( G a s p T ) of the polar solvents adsorbed on the fibers as a function of the temperature (Tables S6 and S7), showing linear variations in ( G a s p T ) and dispersed values depending on the chromatographic methods and molecular models used. Figure 2 shows two examples of the results obtained with the diethyl ether, showing the large difference in ( G a s p T obtained when using the different molecular models and IGC methods in the two studied cases of carbon fibers.
This large difference between the results from the different molecular models and IGC methods can be clearly seen in Figure 2 for the adsorption of diethyl ether on the two carbon fibers (a) and (b) (the other cases of adsorbed polar molecules are shown in Figures S3 and S4). However, the results in Tables S6 and S7, and Figure 2, Figures S3 and S4 show that the oxidized carbon fibers gave larger specific free enthalpy of adsorption of all used polar molecules, demonstrating the higher Lewis acid–base and amphoteric character of the oxidized carbon fiber.
The previous results presented in Figure 2, Figures S3 and S4, as well as those given in Tables S6 and S7, show that the oxidized carbon fibers exhibited greater specific interactions for all the adsorbed polar solvents. This is due to the oxidization of the surface groups of the carbon fibers that increased the acidic and basic surface sites of the carbon fibers and therefore conducted larger specific free enthalpy of adsorption on the oxidized carbon fibers than on the untreated carbon fibers.
The curves in Figure 2, Figures S3 and S4 giving G a s p T versus the temperature for the various polar molecules adsorbed on the carbon fibers following the different models and IGC methods led to the determination of the specific enthalpy and entropy of the adsorption of the polar solvents adsorbed on the carbon fibers. The obtained results are presented in the next section.

3.4. Enthalpic and Entropic Acid–Base Constants

The variations in G a s p T allowed one to obtain the values of specific enthalpy ( H a s p ) and entropy ( S a s p ) of the adsorption of the polar molecules on carbon fibers (a) and (b) for the various models and chromatographic methods. The obtained values of ( H a s p ) are shown in Table 2 and those of ( S a s p ) are shown in Table S8. The determined values of the specific variables varied from one molecular model to the other, with a large deviation. One can conclude that the thermal model gave more accurate results because it took into consideration the thermal effect on the surface area of the organic molecules; this was neglected in the other molecular models (Table 2 and Table S8).
One also confirmed the larger specific enthalpy of adsorption for all polar molecules in the case of the oxidized carbon fibers, thus proving the higher acid–base characteristics.
The Lewis acid–base constants of the two carbon fibers were determined by using relation (3). The variations in H a s p A N and S a s p A N as a function of D N A N are respectively plotted in Figures S5 and S6 for the different IGC methods and models. Figures S5 and S6 show that the linearity of the various curves was not realized for all models and chromatographic methods, except for the Hamieh and Kiselev models. Table 3 and Table 4 show the various values of the enthalpic K A and K D and entropic ω A and ω D acid–base constants of carbon fibers (a) and (b) with the corresponding linear regression coefficient R2. The accurate results obtained by using the thermal model showed an important difference from the other models and methods in terms of the acid–base constants. The smaller values of R2 (<0.500) obtained with the other models led to the belief that these various models cannot be considered accurate. The only interesting result that can be deduced from Table 3 and Table 4 is, confirming once again, the important and greater acid–base constants of the oxidized carbon fibers (b) for the different chromatographic methods and models.
For a comparison between the acid–base constants of the untreated and oxidized carbon fibers, Table 5 shows the corresponding acid–base parameters obtained from the thermal model. The results in Table 6 show that the two fiber types are amphoteric with an important basic character. The ratio KD/KA is equal to 3.1 (about three times more basic than acidic) for the untreated fibers and 5.4 (more than 5 times more basic than acidic) for the oxidized fibers.
One observed that the oxidized fibers are 1.4 times more acidic and 2.4 more basic than the untreated fibers, thus proving the important role of the oxidation of carbon fibers in increasing the acid–base properties. The amphoteric character of the oxidized fibers is about 1.7 more important than that of the untreated fibers.

3.5. Specific and Total Surface Energies of Carbon Fibers

To determine the specific or acid–base surface energy of the studied carbon fibers, one applied the relation of Van Oss et al. [36], given the specific enthalpy of adsorption as a function of the Lewis acid surface energy of the solid surface γ s + and the solvent γ l + , and the corresponding Lewis base surface energy ( γ s for the surface and γ l for the solvent):
G a s p T = 2 N a γ l γ s + + γ l + γ s
In the scale of Van Oss et al. [36], two monopolar solvents, namely, ethyl acetate (EA) and dichloromethane, were used and characterized by
γ C H 2 C l 2 + = 5.2   m J / m 2   ,   γ C H 2 C l 2 = 0 γ E A + = 0   ,   γ E A = 19.2   m J / m 2
By combining the two relations (5) and (6), one can determine the Lewis acid and base surface energies of the solid surface, γ s + and γ s , using the following relations:
γ s + = G a s p T E A 2 4 N 2 a E A 2 γ E A     γ s = G a s p T C H 2 C l 2 2 4 N 2 a C H 2 C l 2 2 γ C H 2 C l 2 +  
By using the experimental results obtained from the thermal model for the application of dichloromethane and ethyl acetate on the two carbon fibers, Table 6 shows the corresponding values of G a s p T at different temperatures.
The values in Table 6 and relations (6) and (7) allowed one to obtain the Lewis acid and base surface energies of the solid surface, γ s + and γ s , as well as the specific surface energy γ s A B of carbon fibers (a) and (b) by using relation (8):
γ s A B = 2 γ s + γ s
The application of relation (8) allowed for the determination of the values of γ s A B of the carbon fibers at different temperatures. Table 7 shows the different values of γ s + , γ s and γ s A B of the untreated and oxidized carbon fibers, γ s and γ s A B (in mJ/m2) of untreated and oxidized carbon fibers.
The obtained values of the specific surface energy γ s A B given in Table 7 show that γ s A B of the oxidized fibers is obviously larger (about 1.5 times) than that of the untreated fibers. The total surface energy γ s t o t . of the fibers can then be obtained by using relation (9):
γ s t o t . = γ s d + γ s A B
The above results of the specific acid–base surface energies of the carbon fibers allowed for the total surface energy of the fibers to be determined by summing the specific surface energy and the dispersive surface energy of the carbon fibers using the results obtained with the thermal model of the two cases where the surface areas of the molecules were calculated by using the PTFE substrate as a model solid (thermal model 1) or PE surface (thermal model 2). The results are given in Table 8.
The results in Table 8 show that the two thermal models reached the same conclusion of a greater total surface energy of the oxidized carbon fiber (b) by about 10% more than that of the untreated carbon fibers, certainly due to the important difference in the values of the specific surface energy between the two fibers because of the increase in the acid–base site numbers in the oxidized fibers. However, when comparing between the magnitudes of the specific acid–base surface energy and the dispersive surface energy of the fibers, one observed that the ratio of γ s A B / γ s d varied between 14% and 20% for the untreated fibers and between 25% and 30% for the oxidized fibers (Figure 3). This is certainly due to the greater percentage of oxygen present in the oxidized form. The results of the chemical analysis of the two carbon fibers determined using XPS measurements are presented in Table 9.

3.6. Comparison with Other Results in the Literature

Many papers have been devoted to the determination of the surface physicochemical properties of activated carbons or carbon fibers by using the inverse gas chromatography technique at infinite dilution.
Schultz et al. [15] determined the dispersive energy components of untreated and oxidized carbon fibers and obtained the values of γ s d = 50 mJ/m2 and γ s d = 49 mJ/m2 at only 320.6 K, respectively. These values cannot be taken into consideration because, as previously mentioned, these authors neglected the thermal effect on the surface area of the solvents and on their surface tensions. Consequently, the values of the acid–base constants cannot be considered accurate. In fact, for the two fiber types, they obtained a more acidic surface, with KA =6.5 and KD = 1.5 for the untreated carbon fiber and KA = 10.0 and KD = 3.2 for the oxidized carbon fiber, while all other models and chromatographic methods showed a higher basic surface for carbon fibers. Later, Menzel et al. [37] found a dispersive surface energy of untreated and oxidized carbon nanotubes equal to γ s d = 94 mJ/m2. In a recent study, Pal et al. [19] found a higher basicity surface of surface-treated activated carbons, with KA ranging from 0.042 to 0.056 and KD ranging from 0.129 to 0.205. They also determined the dispersive surface energy of activated carbons at 140 °C and obtained the values of γ s d for different activated carbons, ranging between γ s d = 213 mJ/m2 and γ s d = 293 mJ/m2 depending on the surface coverage and the activated carbons. However, Pal et al. [19] did not take into account the thermal effect or the variations in the surface tension γ l d of the solvents as a function of the temperature, and they further took G a s p A N instead of H a s p A N by confusing the specific free surface energy G a s p and the specific enthalpy H a s p by neglecting the entropic contribution that was shown to be very important in such cases. By studying various carbon fibers, Liu et al. [18] found a dispersive surface energy of the fibers equal to 40 mJ/m2 and a polar contribution equal to 9 mJ/m2 by using the same previous errors previously mentioned. The superiority of our thermal models resides in the correction of the various values of the surface thermodynamic parameters and variables.

4. Conclusions

In this study, we were interested in the determination of the surface physicochemical properties of untreated and oxidized carbon fibers using the inverse gas chromatography technique at infinite dilution. Experimental measurements allowed for the retention volume of n-alkanes and polar solvents adsorbed on the carbon fibers to be determined. The variations in RTln(Vn) of the adsorbed organic molecules as a function of the temperature led to the determination of the dispersive component of the surface energy of the two carbon fibers and the specific and Lewis acid–base interactions. The results show comparable values of γ s d for the two studied carbon fibers. The specific free energy G a s p T of the adsorption of the polar molecules was determined and showed larger values in the case of the oxidized carbon fibers. The variations in G a s p T versus the temperature allowed for obtaining the values of the specific enthalpy ( H a s p ) and entropy ( S a s p ) of the adsorption of the polar molecules on carbon fibers (a) and (b) for the various models and chromatographic methods. The larger values of ( H a s p ) of the different polar solvents for the oxidized fibers showed that the acid–base site number was greater than that of the untreated fibers, due to the oxidization of the surface groups of the carbon fibers.
The determination of the Lewis acid–base constants indicated that the oxidized fibers were 1.4 times more acidic and 2.4 more basic than the untreated fibers. This proved the important role of the oxidation of the carbon fibers by increasing the acid–base properties. The amphoteric character of the oxidized fibers was shown to be 1.7 more important than that of the untreated fibers.
One also determined the Lewis acid and base surface energies of the solid surface, γ s + and γ s , and therefore the values of the specific acid–base surface energy γ s A B of the carbon fibers at different temperatures. One deduced that the specific surface energy γ s A B of the oxidized fibers was larger (by about 1.5 times) than that of the untreated fibers, confirming the results previously obtained on the strong acid–base interactions of the oxidized carbon fibers with the various polar molecules.
This study clearly shows the non-validity of all methods and models that neglected the effect of temperature on both the surface areas and the surface tensions of organic solvents. A protocol of applied chromatographic methods has to be used while taking into account the thermal effect in all calculations of the various surface thermodynamic parameters and trying to correct the different hypotheses that have been applied for more than forty years.

Supplementary Materials

The following supporting information can be downloaded at: https://0-www-mdpi-com.brum.beds.ac.uk/article/10.3390/cryst14010028/s1, Figure S1. Variations in R T l n V n of the various solvents adsorbed on untreated carbon fibers (a) as a function of the temperature. Figure S2. Variations in R T l n V n of the various solvents adsorbed on oxidized carbon fibers (b) as a function of the temperature. Figure S3. Variations in G a s p of the various solvents adsorbed on untreated carbon fibers as a function of the temperature for the different models and chromatographic methods. Figure S4. Variations in G a s p of the various solvents adsorbed on oxidized carbon as a function of the temperature for the different models and chromatographic methods. Figure S5. Variations in H a s p A N   as a function of D N A N for different molecular models and IGC methods for carbon fibers (a) and (b). Figure S6. Variations in S a s p A N   as a function of D N A N by using the various molecular models and IGC methods for carbon fibers (a) and (b). Table S1. Surface areas of various molecules (in Å2) given by the Van der Waals (VDW), Redlich–Kwong (R-K), Kiselev, geometric, cylindrical or spherical models. Table S2. Values of the surface entropy ε X   ( i n   m J / ( K × m 2 ) ) and γ l   X d 0 K ( i n   m J / m 2 ) of the n-alkanes. Table S3. Normalized donor and acceptor numbers of some polar molecules. Table S4. Values of R T l n V n (in kJ/mol) of the various polar solvents adsorbed on untreated carbon fibers (a) as a function of the temperature. Table S5. Values of R T l n V n (in kJ/mol) of the various polar solvents adsorbed on oxidized carbon fibers (b) as a function of the temperature. Table S6. Values of ( G a s p T ) (in kJ/mol) of the various polar solvents adsorbed on untreated carbon fibers (a) as a function of the temperature by using the various models and IGC methods. Table S7. Values of ( G a s p T ) (in kJ/mol) of the various polar solvents on oxidized carbon fibers (b) as a function of the temperature by using the various models and IGC methods. Table S8. Variations in ( S a s p i n   k J   m o l 1 m o l 1 ) as a function of the used models or methods of polar molecules adsorbed on carbon fibers (a) and (b).

Funding

This research received no external funding.

Data Availability Statement

The data are contained within the Supplementary Material.

Conflicts of Interest

The author declares no conflicts of interest.

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Figure 1. Evolution of γ s d   ( m J / m 2 ) of carbon fibers, untreated (a) and oxidized (b), as a function of the temperature T (K) for the various molecular models.
Figure 1. Evolution of γ s d   ( m J / m 2 ) of carbon fibers, untreated (a) and oxidized (b), as a function of the temperature T (K) for the various molecular models.
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Figure 2. Variations in G a s p of diethyl ether adsorbed on carbon fibers (a) and (b) as a function of the temperature for the different models and chromatographic methods.
Figure 2. Variations in G a s p of diethyl ether adsorbed on carbon fibers (a) and (b) as a function of the temperature for the different models and chromatographic methods.
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Figure 3. Evolution of the different components of the surface energy of the two carbon fibers as a function of the temperature.
Figure 3. Evolution of the different components of the surface energy of the two carbon fibers as a function of the temperature.
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Table 1. Equations γ s d ( T ) of carbon fibers, untreated (a) and oxidized (b), for the different molecular models of n-alkanes, ε s d , γ s d ( T = 0   K ) and T M a x .
Table 1. Equations γ s d ( T ) of carbon fibers, untreated (a) and oxidized (b), for the different molecular models of n-alkanes, ε s d , γ s d ( T = 0   K ) and T M a x .
Untreated Carbon Fibers (a)
Molecular Model γ s d ( T )  
(mJ/m2)
ε s d = d γ s d / d T  
(mJ m−2 K−1)
γ s d ( T = 0 K )
(mJ/m2)
T M a x
(K)
Kiselev γ s d ( T ) = −0.13T + 88.0−0.1388.0702
Spherical γ s d ( T ) = −0.53T + 307.5−0.52307.5586
Geometric γ s d T   = −0.07T + 55.3−0.0755.3848
VDW γ s d ( T ) = −0.14T + 92.7−0.1492.7686
Redlich–Kwong γ s d ( T ) = −0.22T + 152.5−0.22152.5684
Cylindrical γ s d ( T ) = −0.11T + 80.6−0.1180.6739
Hamieh a(T)/PTFE γ s d ( T ) = −0.32T + 174.7−0.32174.7544
Dorris–Gray γ s d ( T ) = −0.16T + 104.0−0.16104.0655
Hamieh–Gray γ s d ( T ) = −0.56T + 272.5−0.56272.5490
Hamieh a(T)/PE γ s d ( T ) = −0.29T + 148.2−0.29148.2503
Global average γ s d ( T ) = −0.26T + 151.2−0.26151.2590
Oxidized Carbon Fibers (b)
Molecular Model γ s d ( T )  
(mJ/m2)
ε s d = d γ s d / d T  
(mJ m−2 K−1)
γ s d ( T = 0 K )
(mJ/m2)
T M a x
(K)
Kiselev γ s d ( T ) = −0.24T + 123.7−0.24123.7517
Spherical γ s d ( T ) = −0.52T + 307.5−0.52307.5586
Geometric γ s d ( T ) = −0.13T + 75.8−0.1375.8576
VDW γ s d ( T ) = −0.26T + 132.9−0.26132.9505
Redlich–Kwong γ s d ( T ) = −0.43T + 218.0−0.43218.0504
Cylindrical γ s d ( T ) = −0.21T + 111.3−0.21111.3536
Hamieh a(T)/PTFE γ s d ( T ) = −0.48T + 223.5−0.48223.5468
Dorris–Gray γ s d ( T ) = −0.16T + 102.7−0.16102.7641
Hamieh–Gray γ s d ( T ) = −0.61T + 287.6−0.61287.6470
Hamieh a(T)/PE γ s d ( T ) = −0.41T + 183.6−0.41183.6449
Global average γ s d ( T ) = −0.36T + 182.5−0.36182.5511
Table 2. Variations in ( H a s p   i n   k J   m o l 1 ) as a function of the used models or methods of polar molecules adsorbed on carbon fibers (a) and (b).
Table 2. Variations in ( H a s p   i n   k J   m o l 1 ) as a function of the used models or methods of polar molecules adsorbed on carbon fibers (a) and (b).
Untreated Carbon Fibers (a)
ProbesCCl4CH2Cl2CHCl3BenzeneEtherTHFEAAcetone
Kiselev1.0751.2006.0110.76512.13512.45611.32116.459
Spherical4.0206.75111.99112.1959.37120.91518.46422.925
Geometric9.51214.04441.5876.6425.82713.83012.56210.470
VDW2.5234.99519.76912.6858.46020.65814.70418.342
R-K2.6015.08119.69112.4948.37020.33114.48318.015
Cylindrical1.54116.59638.802−3.2874.6829.46411.2669.969
Hamieh model1.4751.9006.0111.10013.85213.09318.92313.540
Topological index7.29217.16754.7145.5289.13218.5249.04213.164
Deformation polarizability9.5040.70747.7229.13311.30822.85310.79715.845
Vapor pressure−3.7892.29744.0394.7006.77714.7704.5762.082
Boiling point−4.1670.11041.9134.9909.16213.7964.2624.487
DHvap−3.8392.38242.3474.5847.49512.5402.3022.438
DHvap(T)4.0697.40853.6719.03420.77322.2167.813−4.978
Average values2.4476.20332.9446.1979.79616.57310.80910.981
Oxidized Carbon Fibers (b)
ProbesCCl4CH2Cl2CHCl3BenzeneEtherTHFEAAcetone
Kiselev4.2006.958−18.8953.17016.20320.30016.51228.623
Spherical7.35013.845−11.19716.23213.47729.91424.44135.723
Geometric14.58620.52415.98110.1998.59821.95018.54822.065
VDW6.04511.728−5.15917.18512.30929.98320.58331.148
R-K6.05311.843−4.14016.89212.29229.52120.29430.633
Cylindrical4.98223.65812.922−1.5377.55116.91516.68221.332
Hamieh model4.7822.93711.4162.93117.06320.09930.03924.811
Topological index13.88425.32629.3579.58312.06628.41314.72927.207
Deformation polarizability16.4814.28320.42514.20114.86133.96218.26231.156
Vapor pressure−0.3936.45916.5588.6359.73923.20211.25113.724
Boiling point−0.78911.79912.9898.86412.22022.3859.87416.157
DHvap−0.3386.43313.5558.3849.99220.7727.39613.503
DHvap(T)7.71711.93924.05713.72222.73529.75314.0916.858
Average values6.50512.1339.0679.88213.00825.16717.13123.303
Table 3. Values of the acid–base constants K A , K D , ω A , ω D   and R2 of the untreated carbon fibers (a) with the different acid–base ratios.
Table 3. Values of the acid–base constants K A , K D , ω A , ω D   and R2 of the untreated carbon fibers (a) with the different acid–base ratios.
Models or MethodsKAKDKD/KAR2 10−3ωA10−3ωDωDAR2
Kiselev0.140.292.20.97050.310.411.30.9876
Spherical0.102.5325.30.04750.264.4017.00.0893
Geometric0.051.9943.70.03660.172.9417.70.1959
Van der Waals0.092.4926.70.03750.274.3616.40.0847
Redlich–Kwong0.092.4627.00.03710.244.0416.50.0844
Cylindrical0.12−0.16−1.40.37360.30−0.47−1.60.4863
Hamieh model0.140.443.10.92520.170.754.50.9309
Topological index0.111.6615.10.22640.281.093.80.6131
Deformation polarizability0.132.2117.30.12260.301.695.60.4612
Vapor pressure0.120.695.90.24980.241.154.70.4934
Boiling point0.110.767.10.20890.290.060.20.5289
ΔHvap0.090.707.50.18730.270.090.30.5091
ΔHvap(T)0.141.8913.40.14190.502.434.80.4308
Average values0.141.288.90.31930.301.645.50.5303
Table 4. Values of the acid–base constants K A , K D , ω A , ω D   and R2 of the oxidized carbon fibers (b) with the different acid–base ratios.
Table 4. Values of the acid–base constants K A , K D , ω A , ω D   and R2 of the oxidized carbon fibers (b) with the different acid–base ratios.
Models or MethodsKAKDKD/KAR210−3ωA10−3ωDωDAR2
Kiselev0.200.783.90.72420.341.404.10.8568
Spherical0.163.3421.20.06430.305.9720.10.0689
Geometric0.092.7829.70.060.204.0120.10.1061
Van der Waals0.153.3722.50.05150.335.7717.50.0671
Redlich–Kwong0.150.151.00.05160.305.3317.60.0673
Cylindrical0.180.221.20.74220.38−0.73−1.90.5582
Hamieh model0.191.065.40.980.202.5212.60.9244
Topological index0.172.6015.50.18050.352.687.80.3816
Deformation polarizability0.193.3117.40.11270.383.759.90.2279
Vapor pressure0.171.438.30.20660.370.691.90.4483
Boiling point0.161.549.50.18290.341.063.20.3909
ΔHvap0.151.409.50.16910.310.862.70.3832
ΔHvap(T)0.182.7915.80.1060.464.529.80.2163
Average values0.202.0010.20.25060.352.707.80.3182
Table 5. Values of K A , K D , ω A and ω D   of the two carbon fibers I and II with the acid–base ratios by using Hamieh thermal model.
Table 5. Values of K A , K D , ω A and ω D   of the two carbon fibers I and II with the acid–base ratios by using Hamieh thermal model.
Solid SurfaceKAKDKD/KA10−3ωA10−3ωDωΔA
Untreated carbon fibers (a)0.140.443.10.170.754.5
Oxidized carbon fibers (b)0.191.065.40.202.5212.6
Ratio fibers (b)/fibers (a)1.362.411.741.183.362.80
Table 6. Values of ( G a s p T   in   k J / m o l ) of the dichloromethane and the ethyl acetate adsorbed on carbon fibers (a) and (b) at various temperatures.
Table 6. Values of ( G a s p T   in   k J / m o l ) of the dichloromethane and the ethyl acetate adsorbed on carbon fibers (a) and (b) at various temperatures.
( G a s p ( T ) ) Untreated Carbon FibersOxidized Carbon Fibers
T(K)CH2Cl2Ethyl Acetate CH2Cl2Ethyl Acetate
313.151.27410.6221.27410.622
323.151.25410.2461.25410.246
333.151.2349.8811.2349.881
343.151.2149.4891.2149.489
353.151.1949.0941.1949.094
363.151.1748.7461.1748.746
373.151.1548.4111.1548.411
Table 7. Values of the specific acid and base surface energy contributions γ s + , γ s and γ s A B (in mJ/m2) of untreated and oxidized carbon fibers.
Table 7. Values of the specific acid and base surface energy contributions γ s + , γ s and γ s A B (in mJ/m2) of untreated and oxidized carbon fibers.
In mJ/m2Untreated Carbon FibersOxidized Carbon Fibers
T(K) γ s γ s + γ s A B γ s γ s + γ s A B
313.150.8843.8812.451.0279.7018.06
323.150.8540.7511.790.9574.1916.77
333.150.8237.8211.170.8868.9615.54
343.150.8034.8110.530.8163.8314.35
353.150.7731.919.910.7458.7913.20
363.150.7429.459.350.6853.8612.08
373.150.7227.198.820.6249.0611.00
Table 8. Values of the dispersive γ s d and total γ s t o t . surface energies (in mJ/m2) of untreated and oxidized carbon fibers by using the two thermal models.
Table 8. Values of the dispersive γ s d and total γ s t o t . surface energies (in mJ/m2) of untreated and oxidized carbon fibers by using the two thermal models.
In mJ/m2Thermal Model 1
T(K) γ s d ( F i b e r   a ) γ s t o t . ( F i b e r   a ) γ s d ( F i b e r   b ) γ s t o t . ( F i b e r   b )
313.1574.987.374.392.3
323.1571.082.869.185.8
333.1567.678.764.179.7
343.1563.874.359.373.7
353.1560.270.254.667.8
363.1557.967.250.062.1
373.1556.164.945.556.5
In mJ/m2Thermal Model 2
T(K) γ s d ( F i b e r   a ) γ s t o t . ( F i b e r   a ) γ s d ( F i b e r   b ) γ s t o t . ( F i b e r   b )
313.1556.368.855.974.0
323.1553.064.851.568.3
333.1549.961.147.462.9
343.1546.657.243.357.6
353.1543.553.439.252.4
363.1541.150.435.247.3
373.1538.947.731.342.3
Table 9. Element percentages of the untreated and oxidized fibers.
Table 9. Element percentages of the untreated and oxidized fibers.
Carbon Fiber% C% O% NO/C
Untreated93.125.101.780.055
Oxidized87.3111.071.620.127
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Hamieh, T. The Effect of Temperature on the Surface Energetic Properties of Carbon Fibers Using Inverse Gas Chromatography. Crystals 2024, 14, 28. https://0-doi-org.brum.beds.ac.uk/10.3390/cryst14010028

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Hamieh T. The Effect of Temperature on the Surface Energetic Properties of Carbon Fibers Using Inverse Gas Chromatography. Crystals. 2024; 14(1):28. https://0-doi-org.brum.beds.ac.uk/10.3390/cryst14010028

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Hamieh, Tayssir. 2024. "The Effect of Temperature on the Surface Energetic Properties of Carbon Fibers Using Inverse Gas Chromatography" Crystals 14, no. 1: 28. https://0-doi-org.brum.beds.ac.uk/10.3390/cryst14010028

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