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. 2020 May 5;23(6):101133. doi: 10.1016/j.isci.2020.101133

Anode-Driven Controlled Release of Cathodic Fuel via pH Response for Smart Enzymatic Biofuel Cell

Panpan Gai 1,2, Chengcheng Gu 1,2, Xinke Kong 1, Feng Li 1,3,∗
PMCID: PMC7235283  PMID: 32438288

Summary

Enzymatic biofuel cells (EBFCs) with or without a membrane to separate the anodic and cathodic compartments generally suffered from high internal resistance or interactive interference, both of which restricted the improvement of their performance. Herein, a smart membrane-less EBFC was engineered based on anode-driven controlled release of cathodic acceptor via pH-responsive metal-organic framework ([Fe(CN)6]3-@ZIF-8) nanocarriers. The glucose anodic oxidation would produce gluconic acid accompanied by the change in pH value from neutral to the acidic case, which could drive the degradation of [Fe(CN)6]3-@ZIF-8 nanocarriers and further realize the controlled release of cathodic acceptor [Fe(CN)6]3-. More importantly, compared with controlled EBFC with or without membrane, the power output of the as-proposed EBFC enhanced at least 700 times due to the seamless electronic communication. Therefore, the ingenious strategy not only realized the successful engineering of the membrane-less EBFC but also provided an appealing idea for constructing smart devices.

Subject Areas: Biofuel, Energy Systems, Energy Storage

Graphical Abstract

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Highlights

  • •

    A smart membrane-less enzymatic biofuel cell was fabricated

  • •

    Anode-driven controlled cathodic acceptor release was engineered by pH-responsive nanocarriers

  • •

    The pH-responsive strategy was realized based on [Fe(CN)6]3-@ZIF-8 nanocarriers

Biofuel; Energy Systems; Energy Storage

Introduction

Enzymatic biofuel cells (EBFCs) can convert bioenergy from biochemical reactions directly to electricity and have been widely employed in self-powered biosensors, wearable devices, and implantable power sources (Chen et al., 2019b, Katz and MacVittie, 2013, Miyake et al., 2011, Wu et al., 2017, Xiao et al., 2019). To date, great efforts have been devoted to improving the performance of the EBFC (Fritea et al., 2019, Hickey et al., 2013, Tang et al., 2019). However, a vast majority of them suffered from the long-term coexistence of both anodic and cathodic fuels, which may be prone to interactive interference and the insufficient utilization of biofuels. To address this issue, the membrane was usually introduced to separate the anodic and cathodic chamber (Gai et al., 2016, Gu et al., 2019, Li et al., 2020b, Lv et al., 2018). However, this type of EBFC generally suffered from high internal resistance and lower performance. Even more importantly, it could be not in favor of easy miniaturization platforms or flexible and implantable systems. Thus, it is an urgent demand to develop a new efficient and universal approach for constructing the membrane-less EBFC.

The nanocarrier-controlled release strategy had been widely applied in drug delivery system (Mao et al., 2018, Yang et al., 2019b, Zhang et al., 2016), inspired by which, exploring a suitable nanocarrier would be the critical factor for engineering a smart biofuel cell. Metal-organic frameworks (MOFs) have aroused considerable interest on account of their characteristics of internal volumes and tunable framework chemistries, which exhibited extensive applications in catalysis (Hu et al., 2016, Ma et al., 2014, Wang et al., 2020, Xia et al., 2015, Yang et al., 2019a, Zhang et al., 2014) dynamic therapy (Chen et al., 2018, Lu et al., 2015, Zhang et al., 2018, Zhu et al., 2018), sensing (Chen et al., 2019a, Hu et al., 2017, Kreno et al., 2011, Li et al., 2020a, Ma et al., 2013), as well as drug delivery (Cai et al., 2015, Nazari et al., 2016, Zhao et al., 2016, Zheng et al., 2016). As the typical material, zeolitic imidazolate frameworks 8 (ZIF-8) consisted of Zn2+ ions and 2-methylimidazolate ligand had the unique feature of high stability under the neutral physiological condition but easy to degrade under the acidic condition (Lyu et al., 2014, Mao et al., 2018, Pan et al., 2018, Wang et al., 2017, Yang et al., 2019b, Zheng et al., 2017). For example, Willner et al. utilized the ZIF-8 MOFs as the pH-responsive nanocarriers to realize the controlled release of drugs (Chen et al., 2018, Zheng et al., 2016). Generally, in the anode of the EBFC, glucose could be oxidized to gluconic acid accompanied by the change in pH value from neutral to the acidic case (Katz and Pita, 2009). Thus, ZIF-8 could be an excellent nanocarrier in the controlled-release system based on the glucose oxidation in the anode.

In this context, a smart membrane-less EBFC was engineered based on the anode-driven controlled release of cathodic fuel via pH-responsive ZIF-8 nanocarriers. As shown in Scheme 1, the EBFC was composed of the positively charged cathode and the glucose dehydrogenase/gold nanoparticles (GDH/AuNPs) anode. Initially, in the absence of glucose, the cathodic acceptor [Fe(CN)6]3- was encapsulated in ZIF-8 nanocarriers via a one-pot preparation method, thereby leading to a relatively low power output of EBFC. Once glucose was introduced, the GDH-catalyzed anodic oxidation of glucose produced gluconic acid accompanied by the change in pH value from neutral to the acidic case, which drove the degradation of [Fe(CN)6]3-@ZIF-8 nanocarriers and further caused the release of cathodic acceptor [Fe(CN)6]3- into the electrolyte. Owing to the electrostatic absorption, [Fe(CN)6]3- diffused to the positively charged cathode surface and accepted the electrons generated from the anode to realize the [Fe(CN)6]3- reduction (Equation S1), producing a significantly enhanced power output. Therefore, the smart membrane-less EBFC was realized based on the pH-responsive ZIF-8 nanocarriers. Compared with devices with or without membrane, the power output of the as-proposed EBFCs enhanced at least 700 times due to the elaborate engineering of EBFCs. This ingenious strategy not only avoided long-term coexistence of anodic and cathodic fuels but also efficiently improved the performance of EBFCs, which provided an appealing idea for constructing smart devices.

Scheme 1.

Scheme 1

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Schematic Illustration of the Engineering of Smart EBFC Based on Anode-Driven Cathodic Fuel Release via pH-Responsive ZIF-8 Nanocarriers

Results and Discussion

Characterization of the Anode-Driven System

As the starting switch of the EBFC, the catalytic ability of the anode could be a key factor for the performance of EBFC. Accordingly, AuNPs featured with uniform morphology (transmission electron microscopy [TEM] image in Figure S1) were selected as the substrate materials because of their good biocompatibility and excellent conductivity. Furthermore, electrochemical impedance spectroscopy was employed to investigate the stepwise assembly process of the anode in Figure 1A. The charge-transfer resistance (Rct, 60 Ω) of the AuNPs modified electrode was smaller than that of the bare indium tin oxide electrode (108 Ω) due to the excellent conductivity of AuNPs. When GDH was immobilized onto the AuNPs surface, the Rct sharply increased, being attributed to the fact that the non-electroactive GDH protein shell hindered the redox probes from approaching the electrode surface. Afterward, cyclic voltammetries were performed to study the bioelectrocatalytic behavior of the GDH/AuNPs anode in Figures 1B and S2. The onset potential of the glucose oxidation was about −0.1 V. Furthermore, with the addition of glucose, the oxidation current intensity gradually increased, verifying the efficient glucose oxidation. As a deletional control experiment, the AuNPs had no catalytic current for glucose oxidation in Figure S3. These results demonstrated that the GDH/AuNPs anode with excellent electrochemical performance was successfully fabricated, further confirming the feasibility of the EBFCs launched by the anode.

Figure 1.

Figure 1

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Study of the Anode

(A) Electrochemical impedance spectroscopy of the GDH/AuNPs/ITO anode assembly process.

(B) Cyclic voltammetries of the GDH/AuNPs/ITO anode in 10 mM NaCl solution (pH 7.4) with different glucose concentrations.

Synthesis and Characterization of [Fe(CN)6]3-@ZIF-8 Nanocarriers

[Fe(CN)6]3-@ZIF-8 nanocarriers played a crucial role in the construction of EBFC. Recently, the one-pot method to synthesize organic molecules and proteins encapsulated in ZIFs has been widely studied (Lyu et al., 2014, Zheng et al., 2016). Herein, [Fe(CN)6]3-@ZIF-8 was also synthesized by a one-pot manipulation by adding [Fe(CN)6]3- into the solution of 2-methylimidazole and zinc acetate, which can overcome the traditional drawbacks of tedious multistep procedures and serious leakage. To validate the successful preparation and explore the properties of [Fe(CN)6]3-@ZIF-8 nanocarriers, a series of characterizations were conducted as follows. First, the X-ray diffraction patterns of the [Fe(CN)6]3-@ZIF-8 were almost in accordance with those of the measured patterns of the pure ZIF-8 (5° < 2θ < 30°), illustrating that the encapsulation of [Fe(CN)6]3- had negligible effects on the phase of ZIF-8 hosts (Figure 2A). Also, the energy-dispersive spectroscopy results displayed a clear distribution of Fe, Zn, N, and C elements and the atomic content of Fe was 0.59%, which suggested that Fe element originated from cathodic acceptor [Fe(CN)6]3- was involved in the ZIF-8 nanocarrier (Figure 2B). In addition, TEM showed that the [Fe(CN)6]3-@ZIF-8 basically maintained the rhombic dodecahedral structures similar to pure ZIF-8 with the average particle size of about 150–200 nm (Figures 2C and 2D), demonstrating that the introduction of [Fe(CN)6]3- had almost no effect on the synthesis of ZIF-8. What's more, TEM images displayed that the morphology of [Fe(CN)6]3-@ZIF-8 changed negligibly after 2 days at pH 7.4, suggesting the long-term stability under the neutral condition (Figure 2E). The above-mentioned results demonstrated that the as-proposed [Fe(CN)6]3-@ZIF-8 was successfully constructed by a one-pot method, and exhibited excellent long-term stability under the neutral condition.

Figure 2.

Figure 2

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Study of the [Fe(CN)6]3-@ZIF-8

(A) X-ray diffraction patterns of ZIF-8 and [Fe(CN)6]3-@ZIF-8.

(B and C) (B) Energy-dispersive spectrum and elemental percentage of [Fe(CN)6]3-@ZIF-8. TEM images corresponding to (C) pure ZIF-8.

(D) [Fe(CN)6]3-@ZIF-8.

(E) [Fe(CN)6]3-@ZIF-8 storage for 2 days in 10 mM NaCl solution (pH 7.4).

Feasibility of the Anode-Driven EBFC

ZIF-8 is pH sensitive and easy to degrade under the acidic condition (Chen et al., 2018). To verify whether [Fe(CN)6]3-@ZIF-8 has the same properties, differential pulse voltammetry (DPV) was performed to measure the electrochemical signal of [Fe(CN)6]3- that was released from [Fe(CN)6]3-@ZIF-8 at different pH values. The current responses presented a negative correlation with the pH values ranging from 4.0 to 7.4 (Figure 3A), illustrating that the release of [Fe(CN)6]3- could be well controlled by adjusting pH. The negligible variation of the peak current at pH 7.4 and the stability of [Fe(CN)6]3-@ZIF-8 structure under the neutral condition (Figure 2E) verified that [Fe(CN)6]3- was almost no leak from the nanocarrier. When the [Fe(CN)6]3-@ZIF-8 was treated at pH 4.0, the peak current of [Fe(CN)6]3- had a high value due to the efficient degradation of the nanocarriers, which also could be confirmed by the TEM image (Figure 3D). To realize the pH variation, the GDH-catalyzed anodic oxidation of glucose with different concentrations was performed. As expected, with the addition of glucose concentration, the pH value decreased and reached a plateau when the glucose was up to 50 mM (Figures 3B and S4). Furthermore, the relationship between DPV current values and different glucose concentrations was studied in Figure 3C. It can be seen that the DPV current value of [Fe(CN)6]3- gradually increased with the increase of glucose concentration. Thus, the above-mentioned results strongly verified that the acidic cases caused by glucose oxidation would enable the controlled release of the cathodic acceptor [Fe(CN)6]3-. In the presence of 50 mM glucose, the release amount of [Fe(CN)6]3- was calculated to be 58.5 μM from the DPV linear equation of standard [Fe(CN)6]3- (Figure S5). Meanwhile, the effect of glucose concentration on the structure of [Fe(CN)6]3-@ZIF-8 could also be validated by TEM images. As more glucose was introduced, the frame structure of ZIF-8 was damaged more seriously (Figures 3E and 3F), which also well agreed with the current response of [Fe(CN)6]3-. Overall, the anodic biocatalysis could efficiently regulate the concentration variation of the cathodic acceptor. In addition, the current value of [Fe(CN)6]3- could retain its original signal in the presence or absence of glucose at intervals of 4 days for 20 days, which implied the excellent stability of [Fe(CN)6]3-@ZIF-8 (Figure S6). All the results laid a solid foundation for constructing the anode-driven membrane-less EBFC with excellent performance.

Figure 3.

Figure 3

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Study of the [Fe(CN)6]3-@ZIF-8 Under Different Conditions

(A) DPVs of the [Fe(CN)6]3-@ZIF-8 under different pH values.

(B) pH value variation induced by the GDH-catalyzed anodic oxidation of glucose with different concentrations. Error bars represent the standard deviation of three independent measurments.

(C–F) (C) DPVs of the [Fe(CN)6]3-@ZIF-8 under different glucose concentrations. TEM images of the [Fe(CN)6]3-@ZIF-8 after treatment with 10 mM NaCl solution (pH 4.0) (D) and 5 mM (E) and 50 mM (F) glucose for 30 min, respectively.

Optimization of [Fe(CN)6]3-@ZIF-8 Nanocarriers

The optimization for [Fe(CN)6]3-@ZIF-8 nanocarriers was carried out to maximize the performance of the EBFC, including the concentration and the release time of [Fe(CN)6]3-. First, the concentration of the [Fe(CN)6]3- in [Fe(CN)6]3-@ZIF-8 preparation process was investigated. As depicted in Figure S7A, the peak current increased with increasing concentrations of [Fe(CN)6]3- and tended to level off when the concentration was higher than 3 mM, which suggested that ZIF-8 had a certain loading capacity and reached saturation at [Fe(CN)6]3- concentration of 3 mM. Besides, the effect of the [Fe(CN)6]3- release time was examined to ensure the complete degradation of the nanocarriers. Figure S7B showed that a maximum peak current was obtained up to 3 min, and it barely changed with an even much longer time, indicating that [Fe(CN)6]3-@ZIF-8 could be completely destroyed in 3 min. Hence, 3 min was chosen as the optimal release time.

Anode-Driven Signal Response of EBFC

Based on the above-mentioned analysis, the polarization curves (Figure 4A) and power output curves (Figure 4B) of the anode-driven EBFC with different glucose concentrations were obtained. The results displayed that the open-circuit voltage (EOCV) and the maximum power output (Pmax) of the EBFC showed a positive correlation with the glucose concentration. When the glucose concentration was 50 mM, the EOCV and Pmax reached 0.38 V and 23 μW cm−2, respectively. The internal resistance of EBFC was calculated about 5,790 Ω by Pmax = I2R. To confirm the superior performance of the anode-driven EBFC, a series of deletional control experiments were carried out, in which the EBFCs with or without the membrane were fabricated at the same concentrations of glucose (50 mM) and [Fe(CN)6]3- (58.5 μM). The EOCV and Pmax of the membrane EBFCs were 0.15 V and 0.03 μW cm−2, respectively (Figure S8A), which was much lower than that of the as-proposed EBFC. It might be caused by the high internal resistance of 18,750 Ω originating from the membrane. For the traditional membrane-less EBFCs, the EOCV (7.5 mV) and Pmax (0.07 nW cm−2) were almost negligible (Figure S8B), which was attributed to the fact that there are interferences between the anodic biofuel (glucose) and the cathodic biofuel ([Fe(CN)6]3-). In contrast, the as-proposed EBFC could avoid the interactive interference of the biofuels and enhance the electrical communication between the anode and cathode due to the presence of [Fe(CN)6]3-@ZIF-8 nanocarriers. In addition, the excellent performance of the anode-driven EBFC for different glucose concentrations would also broaden the applications in self-powered glucose biosensors. Herein, the glucose response in as-proposed self-powered biosensors was shown in Figure S9, the linear regression equation was Pmax/μW·cm−2 = 0.374[glucose] + 5.640 (R2 = 0.983) with detection limit of 1.6 mM (3σ/k, where σ is the standard deviation of the blank sample and k is the slope of the analytical calibration). Thus the ingenious EBFC-based self-powered glucose biosensors would be a robust alternative choice for the point-of-care diagnosis.

Figure 4.

Figure 4

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Investigation of the Anode-Driven EBFC

(A) Polarization curves.

(B) Power output curves of the anode-driven EBFC response with different concentrations of glucose.

(C) The selectivity of the anode-driven EBFC in the presence of 50 mM saccharides. ΔP = P – P0, in which P0 was the blank signal of EBFC in the absence of saccharides. Error bars represent the standard deviation of three independent measurements.

(D) Stability analysis of the anode-driven EBFC in the presence and absence of 50 mM glucose in 20 days. Error bars represent the standard deviation of three independent measurements.

Selectivity and Stability of the Anode-Driven EBFC

The specificity of the EBFC was tested by using other three saccharides such as fructose, maltose, and lactose. As depicted in Figure 4C, the interferences with the same concentration showed no obvious signal response compared with glucose, which manifested the good selectivity of the EBFC. Moreover, the long-term stability of the EBFC was also investigated by measuring the Pmax response in the absence and presence of 50 mM glucose every 4 days. It was found that whether the glucose was present or not, EBFC still nearly maintained its original signal in the continuous tests (Figure 4D), demonstrating that the anode-driven EBFC featured with excellent stability.

Conclusion

In summary, a smart membrane-less EBFC was engineered by fully taking advantage of pH-sensitive properties of ZIF-8 and the anodic oxidation of glucose to gluconic acid. Encouragingly, the as-proposed anode-driven cathodic acceptor release system not only significantly decreased the internal resistance but also realized the seamless electronic communication between the anode and cathode. Compared with EBFC with or without membrane in the same conditions, the power output of the anode-driven EBFC enhanced at least 700 times. Overall, the as-proposed strategy provides a brand new idea for the construction of EBFC with high performance and pushes forward the development of smart devices.

Limitations of the Study

Although the smart membrane-less EBFC here was realized based on the pH-responsive ZIF-8 nanocarriers here, the other smart strategy needs to be further explored to get the device higher performance output. Besides, in this study, the implantation of EBFC has not been investigated, which requires more detailed studies.

Resource Availability

Lead Contact

Feng Li lifeng@qau.edu.cn.

Materials Availability

Our study did not generate any new unique reagents.

Data and Code Availability

Our study did not report any unpublished custom code, software, or algorithm.

Methods

All methods can be found in the accompanying Transparent Methods supplemental file.

Acknowledgments

We gratefully appreciate the financial support from the National Natural Science Foundation of China (21605092 and 21775082), the Natural Science Foundation of Shandong Province (ZR2019YQ23), Shandong Province Higher Educational Program for Young Innovation Talents, Major Program of Shandong Province Natural Science Foundation (ZR2018ZC0127), the Research Foundation for Distinguished Scholars of Qingdao Agricultural University (663-1117002), and the Special Foundation for Taishan Scholar of Shandong Province (No. ts201511052).

Author Contributions

C.G. and X.K. planned and performed the experiments. P.G. and F.L. planned and supervised the experiments. All authors discussed the results and participated in the formulation of the manuscript.

Declaration of Interests

The authors declare no competing interests.

Published: June 26, 2020

Footnotes

Supplemental Information can be found online at https://doi.org/10.1016/j.isci.2020.101133.

Supplemental Information

Document S1. Transparent Methods and Figures S1–S9
mmc1.pdf (553.1KB, pdf)

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Associated Data

This section collects any data citations, data availability statements, or supplementary materials included in this article.

Supplementary Materials

Document S1. Transparent Methods and Figures S1–S9
mmc1.pdf (553.1KB, pdf)

Data Availability Statement

Our study did not report any unpublished custom code, software, or algorithm.

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