Compressed, expandable electrodes

Our method overcomes these challenges and provides a new approach for scalable, high-yield graphene production with large sheet size39. As shown in Fig. 1c, rather than a monolithic graphite rod electrode, we utilize graphite flakes without any binder inside a permeable container as the working electrode. Graphite flakes are pressed together by a movable clip on the top to form an electrically conductive electrode. To connect the graphite flakes with the power supply, a piece of platinum wire (current collector) is inserted in the permeable container. This ensures the electrical connection between the graphite flakes and the external pressure created by the clips. A piece of graphite foil works as a counter electrode. The working electrode and the counter electrode are both immersed in an aqueous electrolyte (0.1 M (NH 4 ) 2 SO 4 ). When a positive voltage (+10 V) is applied to the working electrode, the graphite flakes are continuously intercalated and expanded.

Because of the compression of the container, the graphite flakes remain in electrical contact, even as they expand due to gas evolution between atomic layers of graphite flakes. (Note: A simple experiment demonstrates that external pressure is necessary to maintain conductivity throughout the graphite structure, Fig. S1.) The mechanism is the same as the prior work on monolithic graphite rods: the applied voltage drives the reduction of water at the cathode and the hydroxyl ions (OH−) attack graphite at the edges and grain boundaries40,41; the oxidation at the edges and grain boundaries expands the graphite, facilitating the intercalation of sulfate ions (SO 4 2−); the reduction of SO 4 2− anions and oxidation of water generate various gases, such as SO 2 , O 2 , and others. The expanding gases separate the graphene layers, resulting in electrochemically exfoliated graphene (EEG). The counter electrode does not experience any exfoliation. This method is suited to a range of precursor graphitic materials, unlike prior electrochemical methods that require a monolithic graphite structure.

The wetting of the graphite by the electrolyte may be hindered by graphite’s natural hydrophobicity since the reaction involves oxidation only at wetted graphite surface sites. We used HNO 3 to convert hydrophobic graphite to hydrophilic graphite by adding oxygen-containing groups to any pre-existing defect sites (Fig. S2)42. This improved wetting leads to improved ionic transport.

In our batch reactor schematically depicted in Fig. 1c, we introduce graphite flakes (pre-treated as described above) into a tubular dialysis membrane (as the permeable container) and sealed it with two clips (the one on the top is movable). The graphite flakes are electrochemically expanded using the procedure described above. After the process is complete, the resulting product is washed with DI water to remove the electrolyte. We then suspend the product in a vessel filled with DI water where any unexfoliated material rapidly sediments (within 10 minutes). The supernatant from this vessel is collected, and the suspended graphene (the suspension is termed as “EEG-1”) in the supernatant is collected as product. The yield of the process is defined by the ratio of EEG-1 mass to the starting graphite mass. We confirm that this EEG-1 is graphene (distinct from the parent graphite) in more detail below. The EEG-1 may be directly freeze-dried to form graphene powder (the powder is termed as “EEG-2”), or it may be resuspended in DI water and shear mixed (the suspension after shear mixing is termed as “EEG-3”) prior to freeze drying (the freeze-dried powder is termed as “EEG-4”) or vacuum filtration to form a buckypaper (the buckypaper is termed EEG-5) (Fig. S3). (Shear mixing time and speed were varied and are discussed below).

Characterization of as-produced graphene

We utilized atomic force microscopy (AFM) to study the sheet size and thickness of EEG-3. Water-suspended EEG-3 (after electrochemical exfoliation for 4 hours and shear mixing at 8000 rpm, 1 hour) was drop-casted on mica directly for AFM (Fig. 2a,b). The height profile indicates few-layered graphite nanosheets with a thickness between 2–7 nm (Fig. 2c,d). We also used Raman spectroscopy to characterize the structure of EEG-2 and EEG-4 (Fig. 2e). We performed Raman spectroscopy with a 532-nm excitation laser on EEG-2 and EEG-4 pressed on glass slides. The typical Raman spectrum of graphene displays a D peak at 1350 cm−1, a broad G peak at 1580 cm−1, and 2D peak at 2680 cm−1. The shape of the 2D peak identifies the number of layers in graphene43. The G peak corresponds to the first-order scattering of the E 2g mode of sp2 carbon atoms. The prominent D peak is from the breathing mode of the sp2 carbon atoms and activated by the existence of defects, including edges, functional groups (hydroxyl and epoxide groups), and structural disorders. The shape of the 2D peak identifies the number of layers in graphene43. The ratio of D peak to G peak (I D /I G ) varies from 0.9 to 1.2 in different spots. Typically, an I D /I G ratio of 1.2 is very similar to chemically or thermally reduced GO (~1.1–1.5)44. The symmetric 2D peak of our EEG-2 is quite similar to previously reported few-layered graphene. Note that the shear mixing itself does not appreciably alter the Raman signature of the material (Fig. S4). X-ray photoelectron spectroscopy (XPS) was used to probe the chemical composition of the EEG-2 (Fig. 2f–h) (no shear mixing). The EEG-2 shows 16.7 atom % oxygen content. The corresponding C/O ratio of 4.98 for EEG-2 is significantly lower than prior work on electrochemically exfoliated graphene, suggesting a higher degree of oxidation of the parent graphite during the electrochemical exfoliation process1. This occurs because our process is not arrested by the disintegration of the graphite electrode, in contrast to prior studies. The EEG-2 shows less oxygen functional groups than GO from Hummers’ method, but more oxygen functional groups than thoroughly thermal-reduced graphene oxide. This means our EEG-2 has similar chemical/surface properties to partially reduced graphene oxide. Thermogravimetric analysis (TGA) analysis reveals a similar trend (Fig. S5).

Figure 2 (a,b) The AFM height map of EEG-3 deposited on a mica substrate show that the material has a thickness less than 10 nm. (c) and (d) show the height profiles of the lines in (a) and (b), respectively. (e) The Raman spectrum of EEG-2 shows a 2D peak characteristic of graphene. (f) X-ray photoelectron spectra (XPS) of EEG-2 with (g) deconvoluted O 1s and (h) C 1s peaks shows the C/O ratio of the EEG-2. Full size image

To measure the electrical conductivity of the as-prepared EEG-3, we prepared buckypaper via vacuum filtration of the EEG-3 (8000 rpm, 1 hour shear mixing) and this buckypaper is termed as “EEG-5”. This buckypaper showed an electrical conductivity of 2.1 ± 0.2 × 103 S/m, an excellent value similar to that of reduced graphene oxide, demonstrating that the EEG-5 is conductive at levels comparable to prior methods (Fig. S6). We also demonstrate that EEG-4 can be used as a conductive filler in polymer composites. We fabricated a 5 wt.% EEG-4 and polycarbonate (PC) composite using solution-casting and hot-pressing; the resulting electrical conductivity is 2.0 S/m, which is remarkably high compared against other graphene/polymer composites (Fig. S7).

In order to probe the morphology of the produced EEG-2 and EEG-4, scanning electron microcopy (SEM) was performed. Figure 3a shows an SEM image of the parent graphite flakes, which are flat and thick with a mean lateral size of over 1000 µm. Immediately after our electrochemical expansion process, the EEG-2 morphology has a paper-like appearance, with a much higher degree of expansion than in prior methods (Fig. S8). After separation and shear mixing, the resulting EEG-4 sheets consistently show a classic graphene morphology with no unexfoliated material present (Figs 3b, S9). One remarkable aspect of this EEG-3 is the high lateral size, which is even observable in optical microscopy images (Figs 3c, S10). The lateral size of EEG-3 was ~40 µm; this is consistent with additional AFM images (Figs S11, 12). We also observe the expansion of graphite in volume; as shown in Fig. 3d, the freeze-dried EEG occupies a much higher volume than the parent graphite flakes. A leftward shift in the graphite (002) peak in the X-ray diffraction (XRD) spectrum implies disordered restacking of graphene (Fig. S13).

Figure 3 SEM images of (a) parent graphite and (b) EEG-4 (8000 rpm, 1 hour). (c) Bright-field optical microscopy of EEG-3 (1000 rpm, 16 hours). (d) Volumetric change of equivalent masses (0.2 g) of parent graphite on left and EEG-4 on right. Full size image

Scaleup

Yield is one of the most critical metrics for scalable production. Note that the field of graphene production has suffered from a lack of standardization on this point. For example, prior efforts have calculated yield as simply the mass liberated from the graphite electrode divided by the original graphite mass36. This is somewhat misleading, because after the yield is determined, additional sonication and centrifugation (i.e. separation) is needed to produce graphene such that only a fraction of that material actually becomes few-layer graphene. In contrast, we define our yield as the EEG-1 produced after electrochemical exfoliation and sedimentation, with no additional separation steps that reduce the yield; our characterization data above indicate that all of the as-produced EEG-1 can be considered graphene (rather than only a small fraction as in prior methods). Our prototype batch reactor results in yields of 38% (only 15% if the graphite is not pre-treated with HNO 3 ). Below, we show that this number can reach 65% and possibly higher.

The working electrode (graphite flakes compressed in a permeable container) can be modeled as an electrically conductive cylinder (Fig. 4a) where the compressed graphite electrode has a radius of R and a length of L; this roughly corresponds to our initial reactor setup (Fig. 4b,c). The efficiency (η) of the graphite-to-graphene process may drop below 100% because of transport limitations; η is independent of L because the ion transport occurs chiefly in the radial direction. Two key limitations arise: (i) Radial voltage drop will limit the local potential, affecting ion intercalation and oxidation. We ensure the graphite flakes are sufficiently compressed to maintain electrical connection (Fig. S1), and we assume that the electrical resistance of the Pt wire is negligible. As R increases, the average voltage drop from the Pt wire to any given graphite location increases and the efficiency (η) is lowered. (ii) Similarly, ion diffusion into the interior may be the limiting factor; for isothermal ion diffusion-limited reactions, the efficiency η scales with R−1 (regardless of geometry or reaction order) because the Thiele modulus scales linearly with R45. Note that this problem of ion diffusion into the interior is exacerbated as graphite is converted to graphene and the tortuosity increases inside the electrode. (One other potential scaleup limitation is the area of the counter electrode, which must scale with the cross sectional area of the working electrode).

Figure 4 (a) Diagram of the conceptual model of the electrochemical exfoliation process, showing that efficiency of cylindrical electrode exfoliation varies inversely with radius R at large R values. (b) Diagram and (c) picture of prototype batch reactor, with working electrode in an expandable, permeable cylindrical container. (d) Diagram and (e) picture of prototype reactor for forced electrolyte flow through a tileable 2-D graphite electrode with platinized titanium mesh. (f) Schematic for continuous production of EEG in a permeable plug-flow reactor with forced electrolyte flow. Full size image

With these limitations in mind, the electrochemical reactor was redesigned (Fig. 4d,e) to increase the surface-to-volume ratio of the electrode (to reduce ion diffusion limitations), increasing both working electrode and counter electrode area, and decrease electrode separation. To ensure electrolyte transport into the interior of the graphite electrode, a forced electrolyte convection system was fabricated using thermoplastic additive manufacturing. A platinized titanium mesh is inserted into the graphite electrode, which is held in place by filters in an acrylic frame. The counter electrode is a steel grate. This reactor design has the benefit of being infinitely tileable in the plane of the reactor, implying that efficiency is unchanged by scaleup. Utilizing these methods, yield was increased to 65%; this increase indicates that electrolyte diffusion limitations play a major role.

In addition to batch processing, a continuous electrochemical reaction scheme is proposed in which flake graphite is conveyed through a screw reactor and electrolyte is forced under pressure through a porous pipe or ridged mesh (Fig. 4f). These graphite flakes would be in contact with an in-line screw conveyer that doubles as the working electrode, and are continually electrochemically exfoliated as the graphite moves through the reactor. The average exfoliation residence time τ in the continuous reactor is controlled by the graphite flow rate Q and the geometry (area A, length L) of the reactor as τ = AL/Q. This is directly scalable. The flowing graphite must be at a high enough concentration to ensure electrical contact, such that the flow is a dense slurry. This is only one embodiment of the possible continuous electrochemical reactors that uses this compression technique, and many potential designs exist that could lead to efficient continuous graphene production. Additional scaleup factors include: Number, geometry, and material of electrodes and current collectors; parent graphite particle size, and electrolyte distribution systems.