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Carbon Vol. 30, No. 3. pp. 351-357. 1992 000%6223192 %S.(XI + .OO Printed in Great Britarn. Copyright 0 1992 Pergamon Press Ltd. CHEMICAL REACTIONS IN THE STABILIZATION OF MESOPHASE PITCH-BASED CARBON FIBER J. GERARD LAWN Du Pont Fibers, Experimental Station, Wilmington, DE 19880-0302, U.S.A. (Received 12 August 1991; accepted in revised form 25 November 1991) Absbnc&-Mode1 compounds based on anthracene were used to study the chemical reactions taking place during stabilization of mesophase pitch-based carbon fiber. Methyl- and hydro- groups were found to accelerate the oxidation reaction, and also to react with carbonyl groups. Linking reactions that produced high-molecular-weight compounds took place both in air and nitrogen. Similarities in heat- evolution profile were observed in the oxidation of a real pitch and a model pitch consisting of 80% anthracene, 10% dimethylanthracene, and 10% dihydroanthracene. Studies of off-bases produced in stabilization of a pitch-based fiber showed off-gases to be limited to H,O, CO,, and CO (H, would not have been detected). At a given temperature, H,O evolution eventually diminished to zero; however, it could be re-started by increasing temperature. The stabili- zation exotherm was largely associated with H,O production. Carbon-gas production was independent of HZ0 production, and appeared to be a surface reaction. Key Words-Pitch-based carbon fiber, stabilization, Fourier transform infra-red (FTIR), Differential scanning calorimetry (DSC), Thermo-gravimetric analysis (TGA). 1. INTRODUCTION 2. EXPERIMENTAL The process for making carbon fiber from pitch typ- ically involves preparation of a mesophase (liquid crystalline) pitch from residues, converting it into fiber, stabilizing the fiber so that it can be heated above 500°C without melting, and carbonizing at temperatures above 1000°C. Stabilization is the rate- limiting step in the process. While many options exist for stabilization (e.g., reaction with HN03), the method practiced most broadly is thermal oxidation in air or a mixture of air and nitrogen. This reaction is believed to be diffusion limited[l,2]. Two stabi- lization mechanisms are possible: adding oxygen to an organic molecule raises the boiling or melting point (e.g., phenol boils at 182” vs. 80°C for benzene) or, alternatively, oxygen may promote cross-linking between molecules. The chemical and physical processes of stabiliza- tion are complex and poorly defined; the interested reader is referred to a recent survey article[3]. Ox- ygen uptake reactions are believed to occur first at aliphatic side chains to produce a variety of com- pounds by oxygen insertion and dehydrogena- tion[4,5], and further aromatization and cross-link- ing may take place. Gases such as H2, H20, CO, CO*, and CH, have been produced during stabili- zation[6]. Carbon-oxygen reactions have been the subject of extensive study[7,8]. The rate of stabili- zation has typically been studied via Thermo-grav- imetric analysis (TGA)[l]. This work seeks to add to the knowledge base by tracking the oxidation of model compounds by ther- mal analysis, and tracking the oxidation of a pitch fiber by a combination of thermal analysis and infra- red off-gas analysis. It was presented in part at the 20th Carbon Conference[9]. 351 Mixtures of model compounds were made by dis- solving the pure materials in toluene, mixing solu- tions, and evaporating to dryness at room temper- ature. The as-spun carbon fibers used in this study were made from 100% mesophase pitch prepared by the solvent-extraction method[lO]. Differential scanning calorimetry (DSC) was carried out on a Du Pont Model 2100 Thermal Analysis System with a model 910 DSC cell. DSC baseline shift was tracked by alternating periodically between an inert gas (NJ and the oxidizing gas (air), as shown on Fig. 1. Mass spectrometry was carried out on a Vacuum Gener- ator Model 7070 instrument, and Fourier transform infra-red measurements on a Perkin Elmer Model 1800 instrument interfaced with a Du Pont Model 9.51 Thermo-Gravimetric Analyser. 3. RESULTS AND DISCUSSION 3.1 Model compound studies: oxidation reactions Oxidation chemistry was explored using several model compounds based on anthracene: anthracene itself (AC), dimethylanthracene (DMAC), dihy- droanthracene (DHAC), and anthraquinone (AQ). Previous FITR studies showed these moieties to rep- resent the most abundant substituents on the pitch molecule during stabilization. The structure of these compounds is illustrated in Fig. 2. First, the oxidation of pure materials was studied by DSC, at 850 psi pressure, to limit sublimation. DSC profiles of pure compounds ramped at 5°C in air are shown in Fig. 3. AC melted at 215”C, then showed little activity until -3OO”C, where an exo- therm occurred. AQ melted at 282°C and sublimed. DHAC melted at 103”C, then showed three large 352 J. G. LAWN Temperature Time, mins Fig. 1. Stabilization of pitch-based carbon fiber baseline tracking method. exotherms. Finally, DMAC melted at 172°C and a large exotherm followed immediately. Next, the stabilization process was simulated by ramping the samples to 240°C in air and holding for one hour under pressure. AC and AQ melted and sublimed, but did not show an exothermic reaction. Strong exothermic reactions were seen from DHAC and DMAC, almost from the time that heating started (Fig. 4). Mixtures of these compounds were studied next. AC and AQ were treated as base compounds, and DMAC and DHAC as additives, at the 10% level. This level was chosen arbitrarily; however, it rep- resents a 3% level of methyl or aromatic hydrogen groups, which is more than would be expected for coal-tar pitches and less than expected for petroleum pitches. The compositions studied are shown in Table 1. DSC curves for the anthracene-based model com- pounds are shown in Fig. 5. The AC/DHAC curve is very steep, and the reaction is essentially over two minutes after the isothermal temperature was reached. The peak in the AC/DMAC curve was not COMPOUND STRUCTURE CODE Anthracene m AC 0 Anthraqulnone Dlhydroanthracene DHAC Dimethylanthracene DMAC Fig. 2. Structure of model compounds. Fig. 4. Isothermal DSC curves for pure compounds. 10 5 6 P4 3. s ii 1 =2 0 -2 -4 I 50 loo 154 200 250 300 350 400 Temperature, “C Fig. 3. Ramped DSC curves for pure compounds. reached for five minutes after reaching 240°C. The AC/DMAC/DHAC curve was intermediate be- tween the two-not additive! Note that the curve for AC alone is essentially flat; no self-reaction oc- curs at this temperature. DSC curves for anthraquinone-based pitches are shown in Fig. 6. There was no exotherm when the AC/DHAC was heated. There was an exotherm with AQ/DMAC, and a larger one with AQ/ DMAUDHAC. Comparisons with exotherm for the additives alone and the model compounds are shown in Figs. 7 through 9. DMAC alone is com- pared with AC/DMAC and AQ/DMAC in Fig. 7 (the DMAC curve is scaled down from Fig. 4 by a factor of 10). The reaction in DMAC alone was essentially over when the 240°C isotherm was Temp \ \ \ ‘A - 0 --_-___ ._______-_-_-_-_-____ - 140% - E I- Stabilization of a carbon fiber 353 Table 1. Composition of model compounds Antrhacene-based Antrhaquinone-based Ratio AUDMAC AQ/DMAC 90110 AUDHAC AQ/DHAC 90/10 AUDMAUDHAC AQlDMAClDHAC 80/10/10 reached. The AUDMAC exotherm was large and sustained, while the AQ/DMAC exotherm was much smaller in peak value and duration. The AC/ DHAC exotherm is compared with the DHAC exo- therm (scaled by 10) in Fig. 8; the AC/DHAC peak is much larger. The model compounds containing both DMAC and DHAC are compared with a com- posite DMAC + DHAC curve in Fig. 9. Exotherms for the model compounds were approximately twice those for the additives alone. See Table 2. A sensitive method of comparing the reactivityof pitches is to compare the derivative of their heat fluxes as a function of temperature. A comparison is made between a real pitch and the anthracene- based model pitch in Fig. 10. The similarities be- tween the curves are dramatic; the shoulder corre- sponds to the AC/DMAC curve, while the peak corresponds to the ACYDHAC curve. 3.2 Model compound studies: the linking reaction Linking reactions are extremely difficult to study because they are overshadowed by the H,O and car- bon-gas formation reactions. The oxidation of the AQlDMAC mixture suggested that a linking reac- tion might be taking lace. A linking reaction was confirmed by a DSC experiment in which a 50/50 mixture of AQ and DHAC was heated in 300 psi air to 25O”C, and held for an hour. Two reaction peaks were observed in DSC, (Fig. 11) and evidence of high-molecular-weight compounds was found by mass spectrometer (Fig. 12). In subsequent experiments, SO/SO mixtures of DHAC or DMAC were reacted with AC or AQ in nitrogen at 850 psi. Isothermal runs were made, in which the sample was heated to 300°C at SO”C/min., and held, and ramp runs were made in which the Fig. 5. Isothermal DSC curves for anthracene-based mixtures. Fig. 6. Isothermal DSC curves for anthraquinone-based mixtures. sample was heated at SUmin to 400°C. The first surprise came from the DHAC/AC mixture; an exo- thermic peak was observed in the isothermal run, indicating an addition reaction. A rough estimate of the heat of reaction was -10 kcal/mol; this was about 50% of the expected value, but since subli- mation was occurring simultaneously, the true value may be higher. High-molecular-weight material was found in mass spectroscopic analysis of the residue. DHAC reacted with AQ starting at 50°C although no high-MW compounds were found in the residue. DMAC/AC and DMAUAQ mixtures both showed exotherms and gave high-MW compounds; also, each showed 3 melting peaks in the ramped DSC runs. The size of the exotherms was of the order of 10% of the normal stabilization exotherm. 3.3 DSCIFTIR studies on as-spun fibers An experiment was devised to determine the na- ture of stabilization off-gases, and the exotherms associated with them. FTIR and DSC curves were obtained for each sample, using a heating profile which dried the sample at 120°C for one hour, then raised the temperature to 240°C at lO’C/minute and held for five hours. The temperature was next raised to 270°C and held for four hours, then raised to Fig. 7. Comparison of exotherms of mixtures containing DMAC with pure DMAC. 354 J. G. LAWN 300°C and held for three hours. The isothermal hold cycles were based on the author’s estimate of the time required to reduce H,O evolution to zero. Gas evolution is shown in graphic form in Fig. 13 and heat flux is added in Fig. 14. TGA data are shown in Fig. 15. Key observations were: 1. Only CO, C02, and H,O were found in the off-gas (it is possible that Hz was present, but undetected). 2. H,O generation peaked when the sample reached the isothermal temperature, and fell to zero by the end of each cycle, although it could be re- started by raising the temperature. 3. CO/CO, ratios varied between 0.5 and 0.68, with a mean of 0.6, and evolution rates for these gases approximately doubled with each 30°C rise in temperature, falling off slowly with time in each cycle. 4. The exotherm was largely associated with the H,O reaction. 5. Sample weight increased with time until the temperature was raised to 3OO”C, when it decreased. The fact that the H,O evolution went to zero and restarted on heating suggests that at any given tem- Fig. 9. Comparison of exotherms of 3-component model Fig. 10. Comparison of real and model pitches: derivative compounds with theoretical DMAC + DHAC curve. DSC ramp curves. Table 2. Reactivity of the components and model compounds Compound or mixture Ratio Reactivity AC AQ DMAC DHAC loo loo 100 100 AUDMAC ACIDMAC AUDMACYDHAC 90/10 90/10 80/10/10 AQ/DMAC 90/10 AQ/DHAC 90/10 AQ/DMAC/DHAC 80/10/10 None None Strong Strong Strong Strong Strong Weak None Strone perature there are a certain number of reaction sites which eventually become saturated. Previous studies of carbon-oxygen reactions[7] proposed that the mechanism is desorption of carbon-oxygen surface complexes, as gases. The process is characterized by slow buildup of the surface complexes, followed by desorption. The process is illustrated in Fig. 16 by a diagram of gas evolution at the end of the 120”- 240°C heating ramp. The CO, peak did not occur for approximately 10 minutes. By contrast, in later heating ramps, the peak occurred almost instanta- neously. The activation energy for the carbon gas reactions was 11 Kcal/gram mol, compared with a value of 6.4 reported previously[7]. The fraction of CO present in the off-gases is higher than would be expected from previous work[3]; however, temper- atures in this work are considerably lower (240”- 300°C vs. 460”-900”(Z), and burn-off in this work was also very low. 3.3.1 Chemical reactions. Weight losses are due to removal of carbon atoms as CO and CO, and hydrogen atoms as H,O. Weight gain is due to ad- dition of oxygen atoms, and is proportional to HZ0 .05 , , , , , , , ( , , , , , , , , , , , , , ( , Peak Stabilization of a carbon fiber 355 Temperature Reaction Peaks 0.0,’ -HZ0 _._.- CO* ____CO 240°C 270°C 300°C _ 200 400 600 800 Time, mins Fig. 11. Thermal oxidation of AQ/DHAC (50/50) mixture. Fig. 13. Gas evolution during stabilization of pitch-based carbon fibers. generated. The stochiometry of key reactions can be occurred at t = 613 minutes. At this point, gas gen- expressed as follows: eration was as follows: c+~o,-co (1) CO, = 0.477 mg/g/min 2 CO = 0.277 mg/g/min c + 0, - co, (2) HI0 = 0.353 mg/g/min Ar-H + 02- Ar-0 + iH,O + to, From this data we can calculate the loss of carbon and hydrogen: (3) 2 Ar-H + O2 - Ar-0-Ar + H,O (4) Reaction (3) adds one atom of oxygen for each hy- drogen atom produced, whereas reaction (4) adds one atom of oxygen for each two hydrogen atoms produced. w, = Wt(CO*) x $ + Wt(C0) x g 2 + Wt(H,O) x Is = 0.288 mg/g/min (5) At one point in the cycle, the rate of weight gain Assuming reaction (3), oxygen gain is calculated as: was exactly equal to the rate of weight loss. This W, = Wt(H,O) x $ = 0.627 mg/g/min (6) 20* AQ or assuming reaction (4): 60 W, = Wt(H*O) x i = 0.313 mg/g/min (7) The result of eqn (7) is closest to (5) and suggests that two hydrogen atoms are liberated for each ox- 150 200 250 300 350 400 450 500 ygen added. MASS 1.5 I I I 364 EXPANDED SCALE MASS 1 .o 24O’C 270°C 3000 c 200 400 600 800 Time, mins Fig. 12. Mass spectrometer diagram: reaction products of Fig. 14. Heat and water evolution during stabilization of AQ and DHAC. pitch-based carbon fibers. 356 J. G. 112- 110- Time (min) Fig. 15. Weight change during stabilization of pitch-based carbon fibers. "'60 62 64 66 66 70 72 74 76 76 60 62 64 66 68 90 Time (min) Fig. 16. Gas evolution at the end of the first heating ramp. Time. mmr Fig. 17. Ratio of wt. loss/wt. gain during stabilization of pitch-based carbon fibers. Table 3. Average loss/gain ratio for each cycle Cycle temperature Average loss/ (“C) gain ratio 240 0.3 270 1.1 300 2.1 LAWN These results make possible an observation on the use of weight gain data to track stabilization rate[l]. Using eqns (5) and (7), weight loss/gain ratios were calculated for each minute of the cycle described in the previous section, and normalized so that WJW, = 1.0 where dWldt = 0 (the normalization factor was 1.087). The data is shown in Fig. 17 and Table 3. In any given experiment, the loss/gain ratio will depend on pitch type and thermal history. Ex- periments relying on weight gain alone will always understate the rateof oxygen uptake at any mean- ingful stabilization temperature. CONCLUSIONS The model compound work showed that: 1. The oxidation reaction will proceed with an- thracene alone, provided the temperature is suffi- ciently high. 2. The oxidation of anthracene is accelerated by dimethyl- and dihydroanthracene, also the dimethyl- appears to be responsible for the sustained oxida- tion reaction, and the dihydro- for the fast initial reaction. 3. Reactions take place between anthraquinone and dimethylanthracene, and mixtures of dimethyl- and dihydroanthracene, in the presence of oxygen. 4. The correlation between the oxidation of pitch and the model compound AC/DMAC/DHAC (80/ lO/lO) is good. 5. There is a possible linking reaction between anthraquinone and dihydroanthracene. 6. Linking reactions between the compounds take place even in nitrogen, although they are accelerated in the presence of oxygen. Clearly, the abundance of CH2 and CH3 groups in pitches will determine the response of the fiber to stabilization processes. The DSC/FTIR studies of pitch fibers showed that: 1. HZ0 production is independent of CO, and CO production, contrasting with combustion reac- tions, where the gases are byproducts of the same reactions; 2. The decay of H,O production to zero, with subsequent restart on heating indicates a bulk de- hydrogenation reaction, with a limited number of sites available at each temperature; 3. The CO2 and CO production pattern indicates a surface reaction, and the mechanism appears to be desorption of surface oxygen complexes. 4. Tracking weight gain via TGA alone is not a reliable method of determining stabilization kinetics. Acknowledgements-The author gratefully acknowledges the contribution of I. M. Sarasohn, who developed the DSC baseline tracking method and showed the value of com- bined DSCYFI’IR studies. Also acknowledged are stimu- lating mechanistic discussions with H. Kobsa, M. Katz, and Stabilization of a carbon fiber 357 A. D. Kennedy, and the expert assistance of R. A. Twad- 3. S. Lin, SAMPE Journal 27, 9 (1991). dell and J. E. Anderson in thermal analysis and R. E. 4. I. Mochida, A. Azuma, K. Korai, and K. Kitatori, Richardson in FTIR/TGA. 15th Japan Carbon, lA16, 35 (1988). 5. Y. Korai, M. Nakamura, and I. Mochida, Carbon 29, 561 (1991). REFERENCES 6. T. Suzuki, 16th Japan Carbon lAO8, 18 (1989). 7. R. Phillips, F. J. Vastola, and P. L. 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