Characteristics of Activated Carbon Fibers by Chemical Modifications and Thermal Treatments Paper # 1190 Yu-Chun Chiang and Chao-Hsuan Su Department of Mechanical Engineering, Yuan Ze University. 135 Yuan-Tung Rd., Chung-Li, Taoyuan 320, Taiwan, ROC. ABSTRACT Activated carbon fibers (ACFs) are widely used in air pollution control because of their extended surface area, high adsorption capacity, fast adsorption/desorption rates, microporous structure, and specific surface reactivity. Several studies have been attempted to improve the adsorption performance of ACFs. Therefore, the objective of this study is intended to understand the properties of ACFs after chemical oxidations and thermal treatments, and further to evaluate their adsorption capacities. One rayon-based ACF was selected in this study. The fractions of as-received ACF were immersed in H2O2, H3PO4 or HNO3, under room temperature or 60 oC for 1 hour. The thermal treatments were operated in a tubular furnace, carried out at 400, 600 and 850 o C for 30 or 60 min. The properties of ACFs were analyzed, including the surface morphology, the specific surface area, the pore volume, the surface oxides, the ash content and the pH value. The amounts of toluene adsorption on ACFs at 25 oC were determined for evaluation of the effect of chemical modifications and thermal treatments. The results show that the chemical oxidations decreased in specific surface area and pore volume with temperature because parts of the occupation of surface oxides or the collapse of graphitic sheets. Nevertheless, the oxidation followed by thermal treatment would extend the specific surface area and the toluene adsorption of ACFs. But the soaking period of 60 min at 850 oC produced the closure of micropores. The ACFs treated by HNO3 followed with heat treatment possessed much narrow fibers, lower pH values, less ash contents, and better toluene adsorption. The increase of 1 micropore volume after thermal treatment primarily occurred in the neighborhood of indentations or the fiber surface, observed from FE-SEM images. INTRODUCTION Because of their extensive surface area, high adsorption capacity, rapid rates of adsorption/ desorption, microporous structure, and special surface reactivity, activated carbon fibers (ACFs) have been widely used in diverse applications, such as adsorption for pollution control, catalyst and catalyst support, and gas storage. ACFs can be prepared from various precursors like polyacrylonitrile (PAN), rayon, resins and pitches.1 Different precursors would make their final products possess different properties.2 The textural structure and the surface chemistry of ACFs play an important role in ACF applications.3 The pore texture of ACFs depends on the nature of the precursors, the impregnants, flow rate of the reacting gas, maximum heat treatment temperature (HTT) and heating rate.4 Needle-shaped voids have been observed to exist between crystallites in the surface of the PAN fiber.5 The surface chemistry of carbons is determined by the distribution and the nature of the surface functional groups (SFGs) and the heteroatoms. Carbon–oxygen complexes, the most important SFGs,6 are thought to be located near the edges of the polyaromatic sheets in carbon7 or the internal pore/slit/void surfaces and not within the graphitic sheets.8 Lahaye9 and Boehm10 summarized the common methods for characterizing surface oxides, such as acidimetric titration techniques, IR spectroscopy, XPS, thermal desorption spectroscopy, and electrokinetic measurements. It is known that surface oxides on carbon surfaces can be formed by means of thermal treatment at high temperature, ozone treatment, and liquid treatment of the chemical aqueous solution.1 The existence of surface functional groups on carbons such as carboxyl, lactone, phenolic and carbonyl has been postulated as constituting the source of surface acidity.3 A number of treatment methods, including chemical modifications and heat treatments, have been investigated to modify the carbon. For instance, surface oxygen functional groups can be formed on carbons by treatments such as electrochemical oxidation,11 plasma treatment,12 chemical oxidation in HNO3, H2SO4 or inorganic chloride 2 solution,13 and gaseous oxidation with oxidizing gases.13 The gaseous oxidation methods have the advantages of convenience and no significant impacts on physical characteristics of the carbons. Porous carbon materials should be treated at an appropriate temperature to avoid the loss of porosity.14 As HTTs increased, the amount of SFGs was reduced; as a result, the ACFs became more hydrophobic.15 Besides that, the average micropore diameter increased due to the loss of oxygen complexes.8 After ACF was treated above 1100 oC, the degree of graphitization increased significantly. This is partially attributed to the release of the C=O groups.15 Kumar et al.4 suggested that the increase in micropore volume and BET surface area of ACFs under N2 at HTT above 850 oC may be due the formation of new pores. The lower surface area ACFs with smaller pore size possessed higher adsorption capacities for low boiling point alkanes at low concentrations.16 ACFs with different pore texture and surface composition had different adsorption/desorption behavior for polar and non-polar vapors.17 The effects of VOC polarity on the adsorption capacity at lower concentrations were more significant on ACFs with smaller surface areas.17 In addition, SFGs may partially block the pore entrances, altering the rate of diffusion of vapor molecules through the pore system.18 In order to extend their applications, ACFs are usually modified by a variety of surface treatments. There is little information in the literature on how post-treatments, i.e., chemical oxidation followed with heat treatments, affect the physicochemical properties and adsorption capacity of ACFs. Therefore, this study is intended to increase the understanding of the influence of chemical oxidation and thermal treatment on the physicochemical properties of ACFs. A number of techniques have been used to characterize the changes in the carbon surface, and then the adsorption capacities of ACFs have also been determined. EXPERIMENTAL METHODS Activated carbon fibers One rayon-based activated carbon fiber (ACF) sample was used in this study, which was supplied by Taicarbon Inc., Taiwan. It is a non-woven felt with a density of 250 g/m2, a 3 thickness of 2.75 mm, a BET surface area of about 1100 m2/g, a pore volume of 0.45-0.55 cm3/g, and a mean pore diameter of 19-20 Å. The applications suggested by the producers are VOC recovery and waste water treatment. The data of BET surface area, pore volume and pore diameter from the manufacturers are approximate estimates, which are proven in the results section. Carbon (~ 58.42 wt %) is the most abundant element in the as-received ACF samples, and the contents of N and H are 2.57 and 3.58 wt %, respectively. Chemical oxidation and thermal treatment Fractions of as-received ACF, about 20 g in each of the batch, were immersed in H2O2, H3PO4 or HNO3, under room temperature or 60 oC for 1 hour. After that, rinse out the residuals from the ACFs and make ACFs dried. Then the ACF samples were heat-treated inside an alumina combustion tube enclosed in a horizontal tubular furnace under flowing industrial-grade nitrogen gas. After loading the samples the tubular furnace was purged with nitrogen gas for 30 minutes to expel the air inside the furnace tube. Then the samples were heated in an atmosphere of N2 to 400, 600, and 850 oC at a rate of about 15 oC /min. The soaking period was 30 or 60 minutes. After thermal treatment, the samples were cooled in flowing nitrogen gas until they reached ambient temperature. The ACF samples treated are denoted in the text following the rule. The chemical oxidation using H2O2, H3PO4 or HNO3 is denoted as O, P, or N. The time of chemical oxidation treatment at room temperature or 60 oC is denoted as R or H. For example, the ACF samples oxidized by H2O2 at 60 oC for 1 hour and heat-treated at 400 o C for 30 minutes is denoted as OH400-30. Before conducting analyses of surface physicochemical properties and adsorption capacities, the samples were preheated at 103 oC overnight in vacuo to eliminate the contaminants on the surface. Analysis of physicochemical properties Field emission-scanning electron microscope (FE-SEM) images Surface microstructures of ACF samples were observed using the field emission scanning electron microscope (FE-SEM, Hitachi, S-4700, Type II). The specimens of ACFs were coated with a layer of gold or platinum film to enhance the analytical resolution. For each carbon, surface microstructure was inspected with 1000, 5000, 4 10,000 and 100,000 magnifications. Specific surface area and pore texture Adsorption isotherms of nitrogen gas on selected ACF samples were measured with an Accelerated Surface Area and Porosimetry System (ASAP 2010 V4.02), and these isotherms were used to estimate the surface area and the pore texture of ACFs. A small portion of the carbon sample was weighed into a sample tube. Net weight of the carbon sample was about 100 mg after degassing procedures. The purpose of degassing is removal of contaminants from sample surface. During this step the sample was controlled at 250 oC and degas vacuum level of 500 m Hg. The adsorption–desorption isotherm of the nitrogen gas at 77 K was recorded against relative pressures from 0 to 1.0 for a period of about 7–12 hours. Surface areas of the samples were determined by applying the BET and the Langmuir equations to the isotherm data. The amount of nitrogen gas adsorbed at relative pressure near unity was employed to determine the total pore volume. On the assumption that the pores were cylindrical and parallel, the average pore diameter was obtained according to the BET surface area and total pore volume. Surface functional groups (XPS or ESCA) The XPS spectra were obtained with a photoelectron spectrometer (Thermo VG-Scientific, Sigma Probe), also denoted as Electron Spectroscopy for Chemical Analysis (ESCA). A micofocus monochromator Al anode X-ray source was used (h = 1486.68 eV), The survey scans were collected from the binding energy of 0 to 1400 eV, and the high resolution scans were performed over 275-295 eV. For calibration purposes, the C 1s electron bond energy corresponding to graphitic carbon was referenced to 284.5 eV. A Shirley type background was chosen to be subtracted. After the base line was subtracted, the curve-fitting was performed using the non-linear least-squares algorithm under an optimized peak shape. This peak-fitting procedure was repeated until an acceptable fit was obtained. Total ash content The total ash content of ACFs was determined by burning a portion of each carbon in 5 air at 650 oC until constant weight of the residue. The detailed procedures followed the ASTM D2866-94 method.19 The pretreated ACF samples, about 300 mg, were put in the crucible and placed in the muffle furnace at 650 25 oC for about 16 h. The weight percentage of the residue from the original sample is defined as the total ash content. Surface pH value The determination of the pH value of ACFs followed the procedures suggested by the ASTM D3838-80 method.20 A 20-mL portion of boiled de-ionized water was added to a 600-mg ACF sample in the flask equipped with a reflux condenser. The water containing the ACF sample was heated to a boil on a hot plate and boiled gently for 900 10 s. The contents were then filtered immediately. The pH value was determined after the filtrate (10 mL) had been cooled to below 50 5 oC. A triplicate analysis was done for each carbon sample. Adsorption experiments Toluene (C7H8) was selected to evaluate the adsorption capacities of as-received and treated ACF samples. The saturated adsorbed amounts of adsorbate on ACFs were determined according to the ASTM D3467-94 method.21 A small amount of ACF (about 300 mg) was weighed and placed into a U-shaped glass tube. The adsorption temperature was controlled to 25 oC using a water bath. A nitrogen gas purge was blown over the pure liquid VOC solvent such that an expected concentration of VOC was generated continuously. The VOC concentration was controlled between about 1500 ppmv quantified by gas chromatography. The nitrogen gas carried the vapor into a U-shaped sample tube containing a weighed ACF sample. The equilibrium adsorption capacity of ACFs was evaluated after proceeding for 24 hrs. RESULTS AND DISCUSSION Morphology Figure 1 shows the field emission-scanning electron microscope (FE-SEM) images of parts of ACFs samples with a 100,000 magnification. Compared to as-received ACF (in Figure 1a), the microporosity of ACFs can be improved after chemical oxidation or 6 thermal treatment. Especially, for as-received ACF, the micropores probably only occur at the joins of the spunbonded fibers. The post-treatment, oxidation or heat treatment, could generate more micropores at the joins or even on the surface of the fiber (in Figure 1b). The longer period exposed at a specific heating temperature might make the closure of micropores (e.g., Figure 1c and 1d) or the collapse of the microtexture, which was usually observed for the samples treated at room temperature by chemical oxidation. The higher the temperature of thermal treatment, the more the microporosity of the ACFs which have been wet-oxidized (e.g., Figure 1e and 1f). This indicates that the combination of chemical oxidation and thermal treatment can cause the formation of new micropores; but if the period treated is too long, the microstructure would be destroyed and thus to reduce porosity. Figure 1: SEM images of as-received and treated ACF samples with a 100,000 magnification (a) As-received ACF (d) PR400-60 (b) OR600-60 (e) OH850-60 (c) PR400-30 (f) PH850-60 Compare the fiber diameters of the OH-, PH-, NR- and NH-series ACFs, shown in Figure 2, it concludes that chemical oxidation or thermal treatment could reduce the average width of the fibers. Although the oxidative activity of HNO3 is inferior to that 7 of H2O2, HNO3 behaviors a strong corrosion which makes the most narrow diameter of the fibers. For the NH-series samples, chemical oxidations generate a wide variation of the fiber width. The higher the reaction temperature, the more the active reactions. Thermal treatments impose a higher impact on NH-series samples, while their effects on OR- or OH-series samples are quite weakly. Figure 2: Box plots of fiber width (As-received sample: 14 m) Specific Surface Area and Pore Volume The nitrogen adsorption/desorption isotherms at 77 K of selected ACFs samples are shown in Figure 3. All adsorption isotherms appear to be Type I (Langmuir-type), which is indicative of microporous materials. Each isotherm reveals that a hysteresis loop happens, which belongs to the Type H4 of IUPAC classification. Type H4 has been obtained with samples having slit-shaped pores or platelike particles. As P/Po approaches to 1, the curve of the isotherms rise which could be attributed to the occurrence of capillary condensation. 8 Figure 3: Adsorption isotherms of nitrogen gas on selected ACF samples at 77 K Table 1 summarizes the surface characteristics of as-received and treated ACFs estimated from the nitrogen adsorption isotherms at 77 K. Chemical oxidations will eliminate the specific surface area and micropore volume. The reductions are according to the order of HNO3, H2O2, and H3PO4. In addition, the higher the reaction temperature, the more the decrease. After oxidations with HNO3, either at room temperature or 60 oC, followed with thermal treatments would increase the specific surface area and the micropore volume of the ACF samples. However, for the samples treated with H2O2 or H3PO4, followed with a heat treatment at 400 oC for 30 min would generate the lowest specific surface area. In OH-series samples, heat treatments could increase specific surface area of about 11 %. The highest values of specific surface area and micropore volume generally occur at the samples treated at 850 oC for 30 min, except for the NH-series which happens on the sample treated at 850 oC for 60 min. To sum up, NH850-60 possesses the highest values of specific surface area and micropore volume. On the contrary, sample NH has the lowest specific surface area and micropore volume, whose BET is 16 % lower than that of as-received ACF. Any oxidation or thermal 9 treatment process would enlarge the mean pore size. Table 1. Surface micro-structure of ACF samples. Langmuir BET Surface No. ACF OH OH400-30 OH400-60 OH850-30 OH850-60 PH PH400-30 PH400-60 PH850-30 PH850-60 NR NR400-30 NR400-60 NR850-30 NR850-60 NH NH400-30 NH400-60 NH850-30 NH850-60 Area (m2/g) 1086.99 995.06 993.52 1103.61 1184.82 1183.96 1036.61 999.76 1030.56 1037.35 945.53 1001.47 1067.00 1116.10 1190.39 1097.70 909.90 1059.50 1002.30 1155.03 1279.78 Surface Area (m2/g) 1441.67 1317.18 1322.84 1468.21 1582.60 1569.15 1369.32 1321.37 1361.71 1371.65 1248.61 1323.03 1409.97 1477.50 1571.73 1449.90 1204.16 1400.54 1325.26 1527.52 1714.79 Total Pore Mean Pore Size Volume (cm3/g) (Å) 0.5164 0.4760 0.4905 0.5374 0.5842 0.5764 0.5008 0.4775 0.4943 0.4978 0.4477 0.4788 0.5148 0.5385 0.5726 0.5274 0.4382 0.5141 0.4840 0.5571 0.6307 19.0 19.1 19.7 19.5 19.7 19.5 19.3 19.1 19.2 19.2 18.9 19.1 19.3 19.3 19.2 19.2 19.3 19.4 19.3 19.3 19.7 Based on the adsorption isotherms of nitrogen, the distribution of pore volume primarily concentrates on the micropore-size range. Chemical oxidation could make pore become larger or generate more surface oxides, thus reduce the specific surface area and micropore volume. The reduction is related to the oxidant strength or reaction temperature. Low thermal treatment (400 oC) without oxygen would have a further loss of specific surface area and micropore volume. On the other hand, high thermal treatment (850 oC) without oxygen will exhibit a higher specific surface area and micropore volume, due to the generation of new micropore or the decomposition of 10 surface oxygen-containing functional groups. In this case, it needs to be noted that too long reaction time could have an adverse effect on the development of pore structure. Surface Functional Groups XPS data gives information about the composition of the most external surface of ACFs. XPS experiments were performed on three selected samples, i.e., as-received ACF, NH, and NH850-60. The O 1s/C 1s atomic ratios from the survey scans show that the as-received ACF displays a smaller value (0.13). After HNO3 oxidation at 60 oC for 1 hour, the ratio could increase to 0.17. Once continued a thermal treatment at 850 oC for 60 min, the ratio will go up to 17.23. Figure 4 illustrates the high-resolution XPS spectra of the C 1s region. With all carbons, the C1s signal exhibited an asymmetric tailing. This is partially due to the intrinsic asymmetry of the graphite peak and to the contribution of oxygen surface complexes. Deconvolution of the C 1s spectra gives five peaks that represent graphite carbon (peal I, 284.5 eV), carbon present in phenolic, alcohol, ether or C=N groups (peak II, 286.3 eV), carbonyl or quinine groups (peak III, 287.9 eV), carboxyl or ester groups (peak IV, 289.3 eV), and shake-up satellite peaks due to -* transitions in aromatic rings (292.7 eV). The calculated percentages of graphitic and functional carbon atoms are shown in Table 2. There is a slightly increase in the relative content of graphitic carbon and a significant rise in the relative content of carbonyl or quinine groups after HNO3 oxidation at 60 oC for 1 hour. Correspondingly, the relative contents of phenolic, carboxyl, or the carbons present with -electrons are decreased. A dramatic change occurred at sample NH850-60. Compared to as-received ACF, the relative contents of graphitic carbon, and carbonyl or quinine groups increase 27 and 265 %, respectively. The percentage of carboxyl groups decreases 65 %, and the contents of phenolic and carbon with -electrons have been eliminated completely. 11 Figure 4: XPS C1s spectrum of ACFs (a) ACF (b) NH (c) NH850-60 Table 2. The percentages of surface functional groups on ACFs by deconvolution of the C 1s spectra. Surface functional groups Binding energy (eV) As-received ACF NH NH850-60 Graphitic carbon 284.5 68.65 % 68.79 % 86.88 % Phenolic, alcohol, ether or C=N groups 286.3 14.57 % 13.23 % Carbonyl or quinine groups 287.9 2.30 % 4.6 % 8.4 % Carboxyl or ester groups 289.3 13.39 % 12.85 % 4.72 % Carbon present with -electrons 292.7 1.08 % 0.54 % 12 Total Ash Contents Figure 5 gives the total ash content of ACFs. It should be noted that the total ash content of as-received ACF is about 3.75 %; however, the chemical oxidations and thermal treatments will significantly reduce the amount of total ash content. The average ash contents of OH- and NH-series samples are higher than the corresponding OR- and NR-series. This implies that the surface oxides generated during oxidation could prevent the structure from attack during thermal treatment. Aside from the samples treated at 600 oC, the amounts of total ash content of ACFs heat-treated will increase as the reaction temperature or the retention time increases. This could be attributed to the loss of CO, CO2 or other volatiles during thermal treatments; thus, increasing in the content of mineral materials in the residue. Figure 5: Box plots of total ash contents in various series of ACF samples pH Values The as-received ACF has a pH value of 3.27, and after oxidation with H2O2, the pH values will be increased. However, as the samples were oxidized with HNO3 or H3PO4 at 60 oC rather than at room temperature, they could have a higher pH value. The box plots of measured pH values are summarized in Figure 6. As the reaction temperature increases, the pH value increases at first and then decreases, with a maximum value occurs at 600 oC. The increase in the period of thermal treatments generally reduce the 13 pH value, which could be attributed to the occurrence of unstable acidic hydrogen. But when the samples treated at 850 oC, the surface pH values become higher as the treatment duration increases. This finding is speculated on the fact that most of the surface acidic functional groups could have been exhausted under treated at 850 oC. Figure 6: Box plots of pH values of ACF samples after various HTT conditions Adsorption Capacity The equilibrium adsorption amounts of as-received and selected treated ACFs for toluene (C7H8) of about 1500 ppmv at 25 oC were performed. The adsorption amount of toluene on as-received ACF is 30.8 g/100g, but there is a wide variation with progressive treatments. For H2O2-treated ACFs, the adsorption amounts of toluene vary from 5.4 to 42.2 g/100g. For H3PO4-treated ACFs and HNO3-treated ACFs, the values range from 11 to 41.3 and from 14.2 to 48.5 g/100g, respectively. The maximum amount of toluene adsorption occurred on the sample treated with HNO3 at 60 oC for 1 hour and followed with thermal treatment at 850 oC for 60 min. If followed a thermal treatment at low temperature merely after the chemical oxidation, the adsorption capacity of ACFs could not be able to be improved. The adsorption capacities of the samples treated with H3PO4 are compatible with those treated with H2O2 at 60 oC for 1 hour. But the capacities of the samples treated with H3PO4 would be worse when treatments occur at room temperature. The adsorption amounts of toluene on selected 14 ACF samples seem to be related to the calculated BET surface area. Figure 7 illustrates the relationship between the BET surface areas and the adsorption amounts of toluene on the corresponding ACFs samples. It displays a middle degree of correlation between these two parameters. Figure 7: The relationship of BET surface area and adsorption capacity of toluene CONCLUSIONS The results show that the chemical oxidations would decrease in specific surface area and pore volume with reaction temperature. Nevertheless, the oxidation followed by thermal treatment would extend the specific surface area of ACFs. For instance, the specific surface areas of the NR series and NH series increased 18 and 41 %. But the soaking period of 60 min at 850 oC produced the closure of micropores. The increase of micropore volume after thermal treatment primarily occurred in the neighborhood of indentations on the fiber surface, which was observed from the FE-SEM images. Because of high reactivity of HNO3, the ACF samples treated by HNO3 possessed a thinner fiber, a lower pH value, and a less ash amount; but the effect on the amount of 15 surface functional groups was insignificant. The higher the temperature of chemical oxidation, the higher the pH value, and total ash content. With HNO3 oxidation followed by 850oC treated for 60 min, there is an increase in the amount of carbonyl groups on ACFs; however, a significant decrease in the fraction of carboxyl groups has been observed and the amounts of phenolic groups has been completely exhausted. Finally, the amounts of toluene adsorption revealed that the adsorption capacities of ACFs were consistent with the specific surface area and pore volume. REFERENCES [1] Donnet, J.B.; Rebouillat, S.; Wang, T.K.; Peng, J.C.M. Carbon Fibers, Marcel Dekker: New York and Basel, 1998. [2] Edie, D.D. Carbon 1998, 36(4), 345-362. [3] Boehm, H.P. Advances in Catalysis 1966, 16, 179–274. [4] Kumar, K.; Kothari, R.; Bohra, J.N. Carbon 1997, 35(5), 703–706. [5] Johnson, D.J. Journal of Physics D: Applied Physics 1987, 20(3), 287-291. [6] Mattson, J.S.; Mark Jr., H.B. Activated Carbon, Marcel Dekker: New York, 1971. [7] Toles, C.A.; Marshall, W.E.; Johns, M.M. Carbon 1999, 37, 1207–1214. 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[20] ASTM D3838-80, Standard Test Method for pH of Activated Carbon, American Society for Testing and Materials. [21] ASTM D3467-94, Standard Test Method for Carbon Tetrachloride Activity of Activated Carbon, American Society for Testing and Materials. KEYWORDS Activated carbon fiber; Physicochemical property; SEM; XPS; BET; Adsorption 17