Zhipeng Buabc,
Linlin Zangd,
Yanhong Zhang*b,
Xiaojian Caoab,
Liguo Sun*c,
Chuanli Qinab and
Cheng Wang*a
aKey Laboratory of Functional Inorganic Material Chemistry (MOE), Heilongjiang University, Harbin, 150080, China. E-mail: wangc_93@163.com
bSchool of Chemical Engineering and Materials, Heilongjiang University, Harbin, 150080, China. E-mail: zhangyanhong1996@163.com
cKey Laboratory of Chemical Engineering Process & Technology for High-efficiency Conversion, College of Heilongjiang Province, School of Chemical Engineering and Materials, Heilongjiang University, Harbin, 150080, China. E-mail: sunliguo1975@163.com
dState Key Laboratory of Urban Water Resource and Environment, Harbin Institute of Technology, Harbin, 150080, China
First published on 11th May 2017
In this paper, magnetic porous graphene/multi-walled carbon nanotube beads (MPGCBs) were fabricated by a modified capillary microfluidic device. Polystyrene (PS) microspheres not only served as the hard templates to form uniform macropores, but were also beneficial for keeping the stability of spherical architecture. In the process of solidification, both graphene oxide (GO) and acidified multi-walled carbon nanotubes (aMWCNTs) enriched with carboxyl functional groups can form stable and uniform dispersion in the droplets. After the calcination treatment, the composite beads had excellent water resistance and robust mechanical properties. Moreover, due to the addition of the Fe3O4 nanoparticles, the beads also possessed the advantage of flexible operation, which can facilitate oriented movement and recycling of the absorbents, and promoted the collection and recovery of the useful pollutants. These multi-functional MPGCBs with interconnected macroporous structures showed high absorption capacity (up to 8–25 times their own weight) for various kinds of oils and organic solvents, relatively high separation efficiency and long-term recycle stability in the oil/water mixture separation process.
Ball-like particles are not widely used in oil/water mixture separation because few synthetic methods can give them the right structure, size and function. Microfluidics technology could fabricate uniform, monodispersed, spherical beads in the micro-meter to nano-meter diameter, and it has become a means of constructing sophisticated architectures.18–22 Therefore, we utilized a modified droplet-based microfluidic device to obtain a kind of hydrophobic and underwater superoleophilic beads. And the sorbents were designed according to four criteria: (1) the beads should be abundant porosity, moving flexibility and mechanically robust, (2) the beads should be hydrophobic and oleophilic at the same time, (3) the oil/water mixtures should be completely separated, and (4) the beads could be recycled for long-term use. According to the four criteria, we selected graphene and carbon nanotubes as building block to construct the beads. In order to get the high stable beads, beyond the stability of the material itself, the stability of the structure is also very important. Carbon nanotubes are one-dimensional tubular material with a huge aspect ratio and graphene is two-dimensional carbon material composed of hexagonal honeycomb lattice plane. Graphene and carbon nanotubes have similar mechanical properties and their composites can produce structure synergistic effect between them, which lead to stabilize structure and morphology. Compared with the single carbon nanotube beads in our previous report,23 it is believed that the additional graphene play an important role as the “reinforcing walls” to enhance the strength of skeleton structure, and finally leading to the robust mechanical stability of magnetic porous graphene/multi-walled carbon nanotubes beads (MPGCBs).
Herein, we utilized a modified capillary microfluidic method to fabricate MPGCBs. In particular, graphene oxide and acidified multi-walled carbon nanotubes (aMWCNTs) prepared by improved Hummer's method and acid treatment procedure possess abundant carboxyl groups, which can improve their dispersion degree in the droplets and decrease aggregation in the solidification process. After the calcination treatment, hydrophobic surface and porous structure made the MPGCBs possess the ability of absorbing oils or organic solvents either floating on or under water. At the same time, the detailed research about the separating of surfactant-stabilized oil/water emulsions have been studied according to the features of the porous beads, and the high separation efficiency proved that the MPGCBs were suitable for oil/water separation. In addition, through encapsulating magnetic water-soluble Fe3O4 nanoparticles in the emulsion droplets, the porous beads achieved the ability of controlling and facilitating the collection of oil contaminants. And recycled products can be reused through simple combustion method or air distillation process. These unique features will make the magnetic porous beads described here become ideal separation material for water treatment.
The separation experiment was performed on a vacuum-driven filtration system, in which the height of the filtration cell was 80 mm and the diameter of the filter was 15 mm. The sandwich-like filtration membrane was made up of nylon filter membrane and a quantity of MPGCBs (0.25 g), and the schematic diagram of the preparation was shown in Fig. S11.† The diameter of particle-deposited area was 15 mm. The stable emulsion was poured into the filtration cell under a suction vacuum degree at 0.09 MPa.
It can be seen from FTIR spectra of Fig. 3a and S4a† that the characteristic peaks of PS27,28 and the absorption band of carboxyl from GO and aMWCNTs obviously disappeared in MPGCBs, which indicated PS microspheres and part of hydrophilic groups were removed via calcination treatment. Through elemental composition analysis of XPS spectra in Fig. 3b, the similar conclusion can be drawn that MPGCBs had weaker intensity of O 1s peak and relative lower oxygen content than GO/aMWCNTs/PS/Fe3O4 beads. From the C 1s spectrum of MPGCBs (Fig. 3c), three component peaks centering at 284.4, 285.4 and 289.8 eV originated from CC, C–O and CO groups, respectively.29 Due to the small amount of Fe3O4 nanoparticles in MPGCBs, there were no significant peaks in XPS broad spectra. However, XRD patterns (Fig. 3e and S3b†) indicated that there existed a series of peaks located at 30.20°, 35.5°, 43.3°, 53.4°, 57.1° and 62.5°, which related to the (220), (311), (400), (422), (511), and (440) planes of Fe3O4 nanoparticles,30 respectively. The further element state analysis in Fig. 3d showed XPS narrow spectrum had two distinct peaks at 711.0 and 724.0 eV which originated from Fe 2p3/2 and Fe 2p1/2 of Fe3O4 nanoparticles.30,31 The above results confirmed the magnetic property of the synthesized MPGCBs. After pyrolysis treatment, atomic structure or form of carbon materials can be changed and detected via XRD patterns and Raman spectra. In Fig. 3e, a weak peak at 10.70° belonging to the (001) profile of GO sheets29 and the characteristic diffraction band of PS (Fig. S4b†) both disappeared in MPGCBs. And a sharp peak centered at 25.9° in MPGCBs corresponding to the (002) plane of graphitic structure was still maintained.29,32,33 In addition, there were two peaks related to a defect D band at 1362 cm−1 and a broad G band at 1578 cm−1 in Raman spectra of Fig. 3f.34 The presence of D and G bands represented the defect of graphitic structures and the tangential vibration of sp2-bonded carbon atoms, respectively.33 And the intensity ratio between D band and G band (ID/IG) suggested the defect or disordered degree of carbon structures. It can be clearly seen that the ID/IG value of MPGCBs was higher than that of GO/aMWCNTs/PS/Fe3O4 beads, indicating MPGCBs had disorder degree and defects after calcination treatment.
Fig. 3 (a) FTIR spectra, (b) XPS spectra, (e) XRD patterns and (f) Raman spectra of GO/aMWCNTs/PS/Fe3O4 beads and MPGCBs. (c) and (d) were C 1s and Fe XPS spectra of MPGCBs, respectively. |
In order to explore hydrophobic performance of MPGCBs, the wetting behavior was measured via contact angle. It was clearly seen that water droplet with spherical shape stood on the surface of the tiled MPGCBs, and the tested contact angle was 152° (Fig. 4a). This phenomenon manifested that the MPGCBs lost hydrophilic functional groups after pyrolysis treatment, which were endowed with hydrophobic property. As shown in Fig. 4a, when oil droplet was deposited on the MPGCBs, it was absorbed instantaneously and the measured contact angle was around 0°. This result indicated that the interconnected macroporous structure was conductive to absorption of oils and organic solvents, and MPGCBs can be used as absorbents in water treatment field. When used as absorbents for oils and organic solvents, the materials need possess a certain mechanical property. Therefore, two detection modes containing compression and shear flow test were carried out. As shown in Fig. 4b, MPGCBs maintained well shape and no fragmentation phenomenon after loading a 100 g weight. Additionally, the robustness of MPGCBs was investigated under shear flow at different speed (Fig. 4c and Video S1†). The corresponding microscope photographs showed that MPGCBs still kept well sphericity after continuous stirring for 15 min in pure water, even though undergoing the speed of 400 rpm.
The MPGCBs possessed 3D macroporous structure and hydrophobicity, which made it a potential candidate for efficient removal of oils and organic solvents from water. As shown in Fig. S9a,† when a certain amount of MPGCBs were brought into contact with a pump oil layer (dyed with C. I. Pigment Orange) on water surface, they absorbed the oil completely within 30 s. A permanent magnet was utilized to capture the pollutants and pull MPGCBs together for recycling. Furthermore, MPGCBs can absorb organic solvent at the bottom of water such as chloroform (dyed with dark pink) quickly within 20 s (Fig. S9b†). The results suggested that porous structure and magnetic property not only enhanced the efficiency of absorption, but also promoted the collection of absorbents and the recovery of their absorbates.16
In order to further study the absorption capacity quantitatively, here the weight gain (%) is defined as the weight of absorbed substance per unit weight of the pristine MPGCBs.35,36 A series of oils and organic solvents with different surface tension were tested, including the commercial petroleum products (e.g. pump oil), fats (e.g. colza oil), hydrocarbons (e.g. heptanes, n-hexane), aromatic compounds (e.g. toluene), ketones (e.g. acetone), alcohols (e.g. methanol, ethanol, benzyl alcohol) and other organic solvents (e.g. chloroform, DMF), which are common pollutants in our daily life as well as from industry.35–37 It can be seen in Fig. 5 that MPGCBs exhibited a high absorption capacity of 8–25 times its own weight for the aforementioned oils and organic solvents. Importantly, MPGCBs showed higher absorption capacity than many previously reported sorbents, as listed in Table 1, such as activated carbons (<1 time),38 zolite (5 times),39 expanded perlite (3.2–7.5 times)40 and sawdust (3.77–6.4 times),41 PVP–iron oxide NPs (2.6 times),14 magnetic polymer nanocomposites (3.63 times),42 nanosheet-structured boron nitride spheres (NSBNSs) (7.8 times)17 and magnetic porous multi-walled carbon nanotube beads (MCNTBs) (6–18 times).23 Until now, owing to the lack of corresponding reports via microfluidic technology, this work enriched the family of 3D spherical carbon-based absorbents.
Sorbent materials | Absorbed substances | Absorption capacity (g g−1) | Ref. |
---|---|---|---|
Activated carbons | Benzene, toluene | <1 | 38 |
Zolite | ParaLux 701 process oil | 5 | 39 |
Expanded perlite | Crude oil | 3.2–7.5 | 40 |
Sawdust | Fatty acids, vegetable oils | 3.77–6.4 | 41 |
PVP–iron oxide NPs | Crude oil | 2.6 | 14 |
Magnetic polymer nanocomposites | Oils | 3.63 | 42 |
NSBNSs | Pump oil | 7.8 | 17 |
MCNTBs | Oils and organic solvents | 6–18 | 23 |
MPGCBs | Oils and organic solvents | 8–25 | This work |
In W/O emulsions, MPGCBs can also smartly separate oil microdroplets via a homemade vacuum-driven filtration cell. A series of surfactant-stabilized water-in-oil emulsions, including water-in-toluene (S-1), water-in-chloroform (S-2) and water-in-hexane (S-3), were prepared to evaluate the separation capability of MPGCBs. Take S-1 for example, after the emulsion was slowly poured into the container, only toluene selectively passed through the fixed MPGCBs and water was still remained in the membrane surface due to the water-repellency of MPGCBs (Fig. 6A). Optical microscopy images of the original feed and the collected filtrate were taken to characterize the separation effectiveness. As shown in Fig. 6B, numerous water droplets with an average diameter of 190 nm were observed in the feed solution and there were no droplets in the collected filtrate. Optical microscopy images of S-2 and S-3 were provided in Fig. S7.† Briefly, it can be assumed that MPGCBs possessed the outstanding W/O separation performance.
To further evaluate separation efficiency, the water content and oil purity in the collected filtrate were investigated by UV-vis spectrometer and moisture titrator, respectively (Fig. S13 and S14a†). For S-1 emulsion, the characteristic peak of toluene was not observed in the filtrate spectrum (Fig. S13a†), and the oil purity of the collected filtrate can be up to 99.92% (Fig. S14a†). Additionally, S-2 and S-3 emulsions also achieved effective separation and the oil purity were 99.94% and 99.96% in their corresponding filtrate (Fig. S13b, 13c and S14a†). The results indicated the excellent separation efficiency of MPGCBs. As shown in Fig. S14b,† the fluxes of various emulsions permeating through the filtration cell were also measured, and all the fluxes were achieved by calculating the penetrated volume of emulsions in the certain time. For separating W/O emulsions, the viscosity of the oil is a crucial factor, which showed a higher flux for oil with a lower viscosity.43 Three different kinds of oils were chosen to study in our experiment (Table S2†). It can be seen that S-3 emulsion with the lowest viscous presented the highest flux (∼500 L m−2 h−1 bar−1) in all W/O emulsions.
Pollution control and environmental protection efforts require that not only the absorbents are provided with outstanding recoverability, but also the absorbates can be properly recycled and thus reused, because most pollutants are either precious raw materials or toxic, e.g., crude oil and toluene.36,37 According to the features of MPGCBs, there are two common methods containing combustion and distillation for recycling tests. The combustion process was applicable for the effective removal of the flammable and useless pollutants, such as ethanol (Fig. S16a†). And distillation operation was suitable for the recycling of valuable pollutants or those with low boiling points, such as heptane (Fig. S16b†). It can be seen in Fig. 7a that the cyclic combustion test demonstrated that the absorption capacity of MPGCBs after 10 cycles only decreased by 2.58 wt% in comparison with absorption capacity in the first cycle, most likely due to the deposition of residues on the surface or in the internal of the beads after combustion. To demonstrate distillation test, heptane (boiling point, 98.5 °C) was absorbed by MPGCBs. The absorption/distillation process was repeated up to 10 times as well as the combustion process to investigate its recyclability (Fig. 7b). In this test, the beads were heated to 95 °C to release the vapour of heptane.44 It was obviously seen that less than 1 wt% of residual heptane remained after 10 cycles, and the absorption capacity of the beads showed negligible change. The results indicated that MPGCBs had stable absorption capacity and recycling performance.
Fig. 7 (a) and (b) were the recyclability investigation of MPGCBs after combustion and distillation, respectively. |
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c7ra03910g |
This journal is © The Royal Society of Chemistry 2017 |