Chemical Engineering Journal 270 (2015) 168–175 Contents lists available at ScienceDirect Chemical Engineering Journal journal homepage: www.elsevier.com/locate/cej Advanced fabrication and oil absorption properties of super-hydrophobic recycled cellulose aerogels Jingduo Feng, Son T. Nguyen, Zeng Fan, Hai M. Duong ⇑ Department of Mechanical Engineering, National University of Singapore, 9 Engineering Drive 1, EA-07-05, Singapore 117575, Singapore h i g h l i g h t s g r a p h i c a l a b s t r a c t For the first time, paper waste is converted into a green cellulose aerogel by an advanced and costeffective method. The material has high oil absorption capacities of 40–95 times of its weight. The material shows stable superhydrophobicity over five months. Cellulose fiber concentration affects significantly the oil absorption capability of aerogel. The maximum absorption capacity of the aerogel is achieved at 50 °C. a r t i c l e i n f o Article history: Received 14 December 2014 Received in revised form 5 February 2015 Accepted 6 February 2015 Available online 14 February 2015 Keywords: Cellulose aerogel Paper waste Temperature effect Oil spill Absorption Kinetics a b s t r a c t A facile and cost-effective synthesis method of biocompatible cellulose aerogels using recycled cellulose fibers of paper waste and Kymene crosslinker is successfully developed for the first time. After coated with methyltrimethoxysilane (MTMS) via chemical vapor deposition, the recycled cellulose aerogels yields very stable super-hydrophobicity for over five months and excellent oil absorption capacities of up to 95 g g1 with the 0.25 wt.% cellulose aerogel. Effects of different cellulose fiber concentrations, different ratios of the cellulose and Kymene cross-linker composition, ambient temperatures and pH values of the environment on the oil absorption behavior of the cellulose aerogels are also quantified comprehensively. The experimental results show the cellulose aerogels yield the maximum absorption capacity at 50 °C. Compared to the pseudo first-order model, the pseudo second-order model is more validated for the oil absorption kinetics study. The recycled cellulose aerogels are promising for replacing earth-unfriendly polymer-based oil sorbents due to their high oil absorption capacities. Ó 2015 Elsevier B.V. All rights reserved. 1. Introduction With the growth of off-shore petroleum industry and the necessity of marine oil transportation, oil spills have become one of the most important threats to the marine ecosystem. Currently, the methods used for oil spill cleaning can be mainly categorized into ⇑ Corresponding author. E-mail address: [email protected] (H.M. Duong). http://dx.doi.org/10.1016/j.cej.2015.02.034 1385-8947/Ó 2015 Elsevier B.V. All rights reserved. three groups: chemical methods, bioremediation and physical methods [1,2]. Chemical methods including dispersion, in-situ burning and solidification [3] are costly, not environment-friendly. Bioremediation [4,5] using microorganisms to degrade hydrocarbon in the oil, is effective yet time-consuming, and its effectiveness is affected dramatically by temperature, oxygen present and organic species. The physical methods use booms and skimmers to corral the oil [6–8]. However, their efficiency for removing oil remains quite limited. 169 J. Feng et al. / Chemical Engineering Journal 270 (2015) 168–175 In recent years, physical absorption has attracted much attention for the oil spill cleanup issues, owing to its low cost, facile operation and low energy consumption [9,10]. There are basically three categories of sorbents such as natural organic sorbents, inorganic sorbents and synthetic organic sorbents [11–14]. Their effectiveness for oil absorption is commonly evaluated by the mass of oil up taken by per unit mass of the absorbent at its swelling equilibrium [10]. The natural organic sorbents such as rice husk, coconut husk and sugar cane bagasse usually possess the oil absorption capacity of 2–4 g g1 [2,15]. To improve their oil absorption capacity, pyrolysis is used to enhance the porosity of the materials and make them more oleophilic. As a result, the pyrolyzed materials have higher oil absorption ability of 7–10 g g1 [15–18]. Inorganic sorbents such as vermiculite, fly ash and manganese oxide nanofiber membranes have the larger oil absorption capacity of less than 20 g g1 [19,20]. Besides the low oil absorption capacity, these natural organic and inorganic sorbents also suffer the problems of absorbing both oil and water during the absorption process [21]. Such poor hydrophobicity significantly reduces the absorption efficiency in their industrial applications. Several efforts [14,19–31] have been made to develop synthetic organic sorbents with low cost, high oil absorption capacity and good oil–water selectiveness. Commercial polypropylene (PP) fiber mats with excellent hydrophobicity and the oil absorption capacities of approx. 15 g g1 were developed, but their degradation remained a major environmental challenge [14]. To overcome this problem, cellulose aerogels [22–26] composed of biodegradable cellulose fibers and inherited the high porosity and large surface area of aerogels [27,28], were developed as a novel type of the synthetic organic sorbents having the high absorption capacities of over 20 g g1 [29]. The combination of the advanced aerogel properties with the biocompatible cellulose fibers, which are abundant worldwide via woods, plants, algae and animals [30,31], make the cellulose aerogels a very promising candidate for oil absorption applications. The development of recycled cellulose aerogels having low density and high porosity from paper waste were developed through an alkaline/urea method [32,33]. After subsequent hydrophobic coating, the recycled cellulose aerogels showed the very high absorption capacities of 24.4 g g1 for crude oils. These developed cellulose aerogels can reduce further the fabrication cost due to the low cost of the paper waste. In this paper, we report an advanced and cost-effective method to synthesize the recycled cellulose aerogels from paper waste by using Kymene as a cross-linker, instead of sodium hydroxide and urea [24,25,34]. This novel method can reduce significantly the toxicity of raw materials, and the entire synthesis duration from 7 days of previous methods [32,33] down to 2 days. After freezedried and coated with methyltrimethoxysilane (MTMS) via chemical vapor deposition, the recycled cellulose aerogels exhibit ultra-flexibility, highly porosity, super-hydrophobicity and outstanding oil absorption capability. 2. Experiments 2.1. Materials Recycled cellulose fibers and Kymene 557H are sponsored by Insul-Dek Engineering Pte. Ltd. (Singapore) and Ashland (Taiwan), respectively. All the solutions are made with deionized (DI) water. Motor oils of 5w40 and 5w50 are purchased from Carlube and Singer machine oil is purchased from the commercial market. Analytical grade MTMS, sodium chloride (NaCl), hydrochloric acid (HCl), sodium hydroxide (NaOH) and Sudan Red G are purchased from Aldrich Sigma. All these chemicals are used as received. 2.2. Fabrication of the recycled cellulose aerogels The recycled cellulose fibers from paper waste (0.075–0.3 g) and Kymene (5–20 ll) are first dispersed in 30 ml DI water by sonicating the mixtures for 10 min. The suspensions are then placed in a refrigerator at 18 °C for more than 24 h to allow the gelation. The cellulose aerogels are obtained by freeze drying the obtained gels at 98 °C for 2 days using a Scan Vac CoolSafe 95– 15 Pro freeze dryer (Denmark). Thereafter, the cellulose aerogels are further cured at 120 °C for another 3 h to cross-link completely the Kymene molecules. Various cellulose aerogels with different compositions of the cellulose fibers and Kymene are synthesized and summarized in Table 1. Porosities of the aerogel samples are calculated using the following formula. q Ø ¼ 100 1 a ð1Þ qc where qa is the density of the aerogel and qc is the density of crystalline cellulose (1.5 g/cm3) [35]. 2.3. Development of the super-hydrophobic recycled cellulose aerogels As the recycled cellulose aerogels developed in Part 2.2 are hydrophilic, the as-prepared cellulose aerogels are coated with MTMS on their highly porous networks [29,35,36] to form the super-hydrophobic cellulose aerogels for the oil absorption. The cellulose aerogel sample and an open glass vial containing MTMS are placed in a big container. The container is then capped and heated at 70 °C for 3 h for the silanation reaction [33]. After the aerogel structure is coated completely, excessive MTMS is removed by placing the aerogel sample in a vacuum oven until the pressure goes down below 0.03 mbar. 2.4. Characterization Surface morphologies of the developed super-hydrophobic cellulose aerogels (sample A–E) are investigated using a scanning electron microscopy (SEM, JSM-600LV of Japan). Water contact angle measurements are carried out on a VCA Optima goniometer (AST Products Inc., USA) to evaluate the water repellency of the MTMS-coated aerogels. During the test, water drops of 0.5 ll are controlled by the syringe system of the tester, and dispensed drop by drop onto the surface of the samples. The contact angle values are calculated using the contact angle meter software on basis of the droplet shape in the image. For each sample, measurements are repeated at several different positions, and its contact angle is finally determined by averaging these contact angle values from various measurements. To investigate the oil absorption capability of the super-hydrophobic recycled cellulose aerogels, oil absorption test is conducted according to a modified ASTM F726-06 standard. Dry aerogels having dimensions of 45 mm (diameter) 11 mm (thickness) are first weighed, and then immersed in 800 ml motor oil (5w40) for 2 h to ensure a swelling equilibrium. Thereafter, the gels are lifted up from the oil container by a stainless steel mesh basket, drained Table 1 Chemical compositions of various recycled cellulose aerogels. Sample label Cellulose fibers (wt.%) Kymene (ll) Porosity (%) Sample Sample Sample Sample Sample Sample 0.25 0.50 0.75 1.00 0.60 0.60 5 5 5 5 5 20 99.4 98.9 98.1 97.2 n.a. n.a. A B C D E F 170 J. Feng et al. / Chemical Engineering Journal 270 (2015) 168–175 in air for 30 s and weighed again. The oil absorption capacity of the aerogels is calculated using the formula as below: Qt ¼ mw md md ð2Þ where Qt is the oil absorption capacity of the aerogel at time t. md (g) and mw (g) are the aerogel weights before and after the oil absorption, respectively. In order to further study the oil absorption kinetics of these cellulose aerogels, the immersed aerogels are lifted up from the oil, drained and weighted at several time intervals (0, 2, 5, 7, 10, 15, 20, 30 and 60 s). The motor oil (5w50) and the Singer machine oil having different viscosities of 0.14 and 0.026 Pa s, respectively are also used for the absorption kinetics tests to investigate effects of the oil viscosity on the absorption kinetics. 3. Results and discussions 3.1. Morphologies of the super-hydrophobic recycled cellulose aerogels Fig. 1 shows the photographs and SEM images of the developed recycled cellulose aerogels. The aerogel sample in Fig. 1a has a dimension of 45 mm (diameter) 11 mm (thickness) and same shape of its reaction container. As reported previously [33,34], the recycled cellulose aerogels are formed via hydrogen bonding between the self-assembled cellulose fibers. However, in this work, Kymene molecules can diffuse and react with the cellulose fiber surface to form the hydrogen bonding, and also crosslinks with the surrounding Kymene molecules. The utilization of Kymene as a cross linker combines the reinforcement and protection mechanisms [37] during the gelation process, which thus ensure the resultant aerogels with a robust structure and good flexibility. As can be seen in Fig. 1b, the large-scale cellulose aerogel is easily bent or rolled without damaging its shape. However, when the cellulose concentration increases, their flexibility tends to be slightly decreased, as a result of the raised difficulty in sliding and bending of the cellulose fibers. In contrast to the mesopores (2–50 nm) of the aerogels formed by the cellulose nanofibers, highly porous structures of the cellulose aerogels with macropores (>50 nm) can be clearly observed in SEM images of Fig. 1c–f. Their macropores are possibly caused by the larger size of the recycled cellulose fibers, obtained from the paper waste [33]. Fig. 1c and d shows the morphologies of the cellulose aerogels with cellulose concentrations of 0.25 and 1.00 wt.% respectively. The aerogel with the higher cellulose concentration (1.0 wt.%) has a more compacted network and lower porosity. However, an increase of Kymene from 5 to 20 ll in a 30 ml reaction mixture does not significantly impact the aerogel structures as shown in Fig. 1e and f. In order to investigate the super-hydrophobicity of the developed cellulose aerogels, the water contact angles are measured on both the external and internal surfaces of the MTMS-coated cellulose aerogels. As shown in Fig. 2a and b, the large contact angles of 153.5° and 150.8° are obtained respectively, thus proving that the hydrophobic coating is successfully covered the whole aerogel networks. The effects of reagent ratios on the super-hydrophobic properties of the aerogels with different compositions are also presented in Fig. 3. Interestingly, all cellulose aerogels exhibit similar Fig. 1. (a) Super-hydrophobic recycled cellulose aerogel, (b) flexibility of the large-scale cellulose aerogel (38 cm 38 cm 1 cm) containing 0.60 wt.% of the cellulose fibers, SEM images of the cellulose aerogels with different ratios of cellulose fibers (wt.%) and Kymene (ll): (c) 0.25:5, (d) 1.00:5, (e) 0.60:5 and (f) 0.60:20. Fig. 2. Water contact angles on (a) the external surface and (b) the cross section of the super-hydrophobic recycled cellulose aerogel. 171 J. Feng et al. / Chemical Engineering Journal 270 (2015) 168–175 confirm the uniform MTMS coating, the excellent hydrophobicity stability of the MTMS-coated recycled cellulose aerogels in this work. 3.2. Oil absorption capabilities of the recycled cellulose aerogels Fig. 3. Effects of exposure time on the water contact angles: (a) of the cellulose aerogels with different ratios of the cellulose fibers and Kymene, and (b) on the external surface and the cross section of the same aerogel. water contact angles of approx. 150°, regardless of their cellulose concentrations or Kymene amount in Fig. 3a. It is well-known that the water contact angles strongly depend on the functional groups on the aerogel surfaces. Therefore, in this case, such a small variation may likely be a consequence of the identical functional groups (ASiAOACH3A) induced by the MTMS coating [33]. To examine the hydrophobic stability of the cellulose aerogels, they are then exposed in normal ambient atmosphere for five months. Their water contact angles of 145–155° over the period are examined as can be seen in Fig. 3a and b. Apparently, their water contact angles on the external surface and the cross section do not show any obvious change with time. These results further Table 2 Viscosities of the tested oils at different temperatures. Viscosities (Pa s) 25 °C 50 °C 70 °C 5w40 motor oil 5w50 motor oil Singer machine oil 0.140 0.160 0.026 n.a. 0.054 0.009 n.a. 0.029 0.006 A 5w40 motor oil is used to investigate the oil absorption capabilities of the recycled cellulose aerogels in Table 2. When the Kymene amount is kept to be 5 ll and increasing the cellulose concentration from 0.25 to 1.00 wt.%, the measured absorption capacities of the aerogels A–E in Table 2 are 95, 73, 58 and 49 g g1, respectively at 25 °C. The maximum absorption capacity of 95 g g1 is achieved with the 0.25 wt.% cellulose aerogel due to its lowest density (7 103 g/cm3) and highest porosity (99.4%). The absorption capacities of all the MTMS-coated cellulose aerogels are one order greater than those of the nature sorbents, 2–4 times greater than those of the commercial polypropylene sorbents [13–15], and also 5 times higher than those of the recycled cellulose aerogels (20 g g1) reported by the previous works using the sodium hydroxide/urea method [32,33]. The significant enhancement of the absorption capacity may be largely ascribed to the reduced densities and increased porosities of the cellulose aerogels. Without using urea and hydroxide residuals, the densities of the cellulose aerogels cross-linked by the Kymene are consequently lowered with their weights. 3.3. Effects of the cellulose fiber concentrations, oil types and temperatures on the oil absorption kinetics of the recycled cellulose aerogels The absorption kinetics of the 5w50 motor oil and Singer machine oil onto the recycled cellulose aerogels are investigated and summarized in Table 3. Although sample A with cellulose fiber concentration of 0.25 wt.% (Table 1) has the highest oil absorption capacity, it possesses a weak mechanical strength and is easily to disintegrate after absorbing oil. Therefore, three different aerogel samples marked as B, C and D (Table 1) having cellulose fiber concentrations of 0.50, 0.75 and 1.00 wt.% are prepared for the oil absorption kinetics tests at 25 °C. As shown in Fig. 4, the sorption capacity of each oil on the cellulose aerogels is plotted as a function of absorption time. The sorption rate is fast at the first 10 s and the absorption reaches the equilibrium state at 30 s for both of the two oils. Temperature is also the major factor affecting the viscosity and the diffusion rate of the oils into the porous aerogel structures. Therefore, the absorption behavior of the different oils on each aerogel is examined at three different temperatures of 25, 50 and 70 °C. As shown in Fig. 5 and Table 3, the maximum oil absorption capacity Table 3 Summary of the maximum oil absorption capacities and the absorption rate constants at different temperatures of the cellulose aerogels having various cellulose fiber concentrations using the pseudo-first and -second order models. ⁄ Cellulose concentration (wt.%) 0.50 Temperature (°C) 25 50 70 25 50 70 25 50 70 5w50 motor oil Maximum absorption capacity, Qm (g/g) Pseudo-first order R2⁄ k1 Pseudo-second order R2⁄ k2 62.6 0.9858 0.2929 0.9955 0.0056 64.9 0.9701 0.3235 0.9962 0.0082 59.2 0.9717 0.3552 0.998 0.0098 48.1 0.977 0.2539 0.9946 0.0075 53.8 0.9544 0.3187 0.9978 0.0098 46.3 0.9658 0.3671 0.9964 0.0153 45.9 0.9857 0.2176 0.9956 0.0048 46.5 0.9926 0.2866 0.9949 0.0066 46.2 0.9437 0.3574 0.998 0.0133 Singer machine oil Maximum absorption capacity, Qm (g/g) Pseudo-first order R2⁄ k1 Pseudo-second order R2⁄ k2 59.3 0.9825 0.2965 0.9942 0.0075 61.0 0.978 0.3110 0.9992 0.0101 58.2 0.9803 0.3514 0.9987 0.0123 46.1 0.9808 0.2734 0.9964 0.0083 48.8 0.9557 0.3063 0.995 0.0113 47.6 0.9935 0.3432 0.9989 0.0146 40.4 0.9782 0.2782 0.9929 0.0070 43.1 0.9704 0.3768 0.9936 0.0092 42.4 0.9871 0.4252 0.9959 0.0161 R2 is the correlation coefficient. 0.75 1.00 172 J. Feng et al. / Chemical Engineering Journal 270 (2015) 168–175 increases when increasing the temperature from 25 to 50 °C, but then decreases with the temperature change from 50 to 70 °C. This trend occurs to the absorption behavior of all the oils on the 0.50, 0.75 and 1.00 wt.% cellulose aerogels. It may be explained that the temperature increase can reduce the oil viscosity in Table 2, which facilitates oil penetration into the porous aerogel networks. However, the low viscosity of the oils has a negative effect on their anchoring to the pore walls, which reduces the amounts of the oil retained in the porous absorbents. Comparing the maximum oil absorption capacity to the tested temperatures, it can be concluded that 50 °C is the optimum temperature for the oil absorption performance of the recycled cellulose aerogels. Beside the temperature effects, the porous structure of the cellulose aerogels also significantly affects their oil absorbency. Fig. 5 and Table 3 show the oil absorption capacity of the aerogels reduces when the initial cellulose concentration increases from 0.50 to 1.00 wt.%. It can be explained based on the porosity of the cellulose aerogels. Table 1 shows the aerogel porosity reduces from 98.9% to 97.2% when the cellulose concentration increases from 0.50 to 1.00 wt.%. As the aerogel porosity is lower, there is less space in the aerogel network for oil occupation and therefore, the oil absorbency is less. Various kinetics models have been suggested for absorption analysis [38–40]. The pseudo-first order and pseudo-second order models [11,41–44] are commonly used for the oil absorption. In this work, both of the models are used to fit the experimental absorption kinetics data. After integration, the pseudo-first order equation can be obtained [41]: ln Fig. 4. Absorption kinetics of (a) the 5w50 motor oil and (b) the Singer machine oil onto the recycled cellulose aerogels with various cellulose fiber concentrations of 0.50, 0.75 and 1.00 wt.% at 25 °C. Qm ¼ k1 t Qm Qt where Qm (g/g) is the maximum oil absorbency, Qt is the oil absorbency at time t, and k1 is the absorption rate constant determined from the slope of ln[Qm/(Qm Qt)] versus t plot. And the pseudo-second order equation can be converted into a linear form [40]: t 1 1 ¼ tþ Qt Qm k2 Q 2m Fig. 5. Maximum absorption capacities, Qm of (a) the 5w50 motor oil and (b) the Singer machine oil onto the recycled cellulose aerogels with various cellulose fiber concentrations of 0.50, 0.75 and 1.00 wt.% at 25, 50 and 70 °C. ð3Þ ð4Þ By plotting (t/Qt) versus t, the absorption rate constant k2 can be determined. The pseudo first-order model can be used in many absorption cases, such as systems close to equilibrium, systems with time-independent solute concentration or linear equilibrium absorption isotherm [40] while the pseudo second-order model is used to describe the sorption process controlled by chemisorption [39,42,45–48]. For the absorption of the 5w50 motor oil and Singer machine oil on the 0.50 wt.% cellulose aerogel at 25 °C, respectively, Fig. 6a and b shows the plots of ln[Qm/(Qm Qt)] versus time t using the pseudo-first order model while Fig. 6c and d displays the plots of (t/Qt) against t using the pseudo-second order model. Fig. 7a and b shows the experimental absorption kinetics data the two fitting model curves for the absorption of the two oils on the 0.50 wt.% aerogel samples. From the plots of Fig. 6, the sorption rate constants k1, k2 and the correlation coefficient R2 are calculated and presented in Table 3. It can be seen that the correlation coefficient values of the pseudo second-order model are higher than those of the pseudo first-order model for both tested oils. So the pseudo secondorder model can predict better the oil absorption behavior in this work. Most of the absorption rate constants k1 and k2 for the 5w50 motor oil are smaller than those for the Singer oil. This means the oil absorption of the Singer oil occurs faster due to its lower viscosity. Activation energy, Ea is an important parameter in a thermodynamic study [49]. In absorption, the energy must be overcome by J. Feng et al. / Chemical Engineering Journal 270 (2015) 168–175 173 Fig. 6. Pseudo-first order absorption linear fitting of (a) the 5w50 motor oil and (b) the Singer machine oil and Pseudo-second order absorption linear fitting of (c) the 5w50 motor oil and (d) the Singer machine oil onto the aerogel having 0.50 wt.% of the cellulose fibers at 25 °C. lnk ¼ lnA Ea RT ð5Þ where A is the pre-exponential factor and R is the gas constant (8.314 J/mol K). By plotting ln[k] against 1/T, Ea can be calculated from the slope. Plots of ln[k1] and ln[k2] versus 1/T are presented in Fig. 8a–d and the activation energy values are presented in Table 4. It can be observed that the activation energy values of the pseudo second-order model are higher than those of the pseudo first-order model. This is because the pseudo second-order model is used for the absorption process controlled by chemisorption, which involves higher forces than in physic-sorption [39]. Compared to the 5w50 motor oil, the Singer machine oil has the lower activation energy values which make the oil absorption on the cellulose aerogels more effective. 3.4. Effects of environmental conditions on the oil absorption performance of the recycled cellulose aerogels Fig. 7. Experimental data fitted with the pseudo-first and -second order models for the absorption kinetics of (a) the 5w50 motor oil and (b) the Singer machine oil onto the aerogel having 0.50 wt.% of the cellulose fibers at 25 °C. an absorbate to interact with functional groups on the sorbent surface. The activation energy can be determined from the change of the absorption rate constant, k with temperature, T (K) using the Arrhenius equation [38,49]: To evaluate the practical oil absorption performance of the recycled cellulose aerogels in the sea, a 3.5% NaCl solution is prepared to imitate the artificial seawater. Fig. 9 depicts the absorption process in the first several minutes. It is visible that the cellulose aerogel is loaded on the top of the mixture and quickly absorbs the motor oil within 7 min. Also the pH effects on oil absorption capacities of the cellulose aerogels are investigated by using the artificial seawater with different pH values prepared from HCl or NaOH. The oil absorption capacities of the 0.50 wt.% cellulose aerogels under the pH = 3, 5, 7 and 9 environment are measured to be 63.00, 62.85, 63.06 and 62.98 g g1, respectively, The absorption results indicates a pH-insensitive behavior of the aerogels during the oil absorption tests. This may be possibly because the oil capacities of the aerogels are mostly contributed by their porosities and tested oil viscosities, while both of them are independent on the environmental pH values. 174 J. Feng et al. / Chemical Engineering Journal 270 (2015) 168–175 Fig. 8. Plots of ln(k1) and ln(k2) against reciprocal temperature for the absorption of (a and b) the 5w50 motor oil and (c and d) the Singer machine oil, respectively onto the cellulose aerogels with various cellulose fiber concentrations of 0.50, 0.75 and 1.00 wt.%. Table 4 Activation energies of the absorption of the cellulose aerogels having various cellulose concentrations on the oils using the pseudo-first and -second order models. Activation energies, (J/mol) Initial cellulose concentration (%) 0.50 0.75 1.00 5w50 motor oil Pseudo-first order Pseudo-second order 3609.6 10682.7 6984.6 13120.3 9331.6 18612.6 Singer machine oil Pseudo-first order Pseudo-second order 3090.5 9354.9 4248.0 10610.3 8130.2 15240.4 Fig. 9. Oil absorption process of the recycled cellulose aerogel having 5.0 wt.% of the cellulose fibers in the artificial seawater (3.5% NaCl and pH = 7) mixed with the 5w40 motor oil and dyed with Sudan Red G before testing. 4. Conclusions In conclusion, an advanced and cost-effective method of the recycled cellulose aerogels from paper waste is successfully devel- oped. After coated with MTMS, the developed cellulose aerogels exhibit excellent oil absorption capacities and very stable superhydrophobicity for over five months. It is found that the initial cellulose fiber concentration significantly affects the oil absorption J. Feng et al. / Chemical Engineering Journal 270 (2015) 168–175 capability of the developed cellulose aerogels. The 0.25 wt.% cellulose aerogel yields the maximum absorption capacity of 95 g g1 with the 5w40 motor oil. The maximum absorption capacity of the cellulose aerogels can be achieved at 50 °C, regardless the pH values of the seawater/oil suspensions and decreases with the increase of the cellulose fiber concentration. The pseudo-first and -second order kinetics models are applied to describe the oil absorption behavior of the recycled cellulose aerogels for the first time. 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