Evaluation of the technoeconomic feasibility of electrochemical hydrogen peroxide production for decentralized water treatment

Yang Li , Yixin Zhang , Guangshen Xia , Juhong Zhan , Gang Yu , Yujue Wang

Front. Environ. Sci. Eng. ›› 2021, Vol. 15 ›› Issue (1) : 1

PDF (1574KB)
Front. Environ. Sci. Eng. ›› 2021, Vol. 15 ›› Issue (1) : 1 DOI: 10.1007/s11783-020-1293-2
RESEARCH ARTICLE
RESEARCH ARTICLE

Evaluation of the technoeconomic feasibility of electrochemical hydrogen peroxide production for decentralized water treatment

Author information +
History +
PDF (1574KB)

Abstract

• Gas diffusion electrode (GDE) is a suitable setup for practical water treatment.

• Electrochemical H2O2 production is an economically competitive technology.

• High current efficiency of H2O2 production was obtained with GDE at 5–400 mA/cm2.

• GDE maintained high stability for H2O2 production for ~1000 h.

• Electro-generation of H2O2 enhances ibuprofen removal in an E-peroxone process.

This study evaluated the feasibility of electrochemical hydrogen peroxide (H2O2) production with gas diffusion electrode (GDE) for decentralized water treatment. Carbon black-polytetrafluoroethylene GDEs were prepared and tested in a continuous flow electrochemical cell for H2O2 production from oxygen reduction. Results showed that because of the effective oxygen transfer in GDEs, the electrode maintained high apparent current efficiencies (ACEs,>80%) for H2O2 production over a wide current density range of 5–400 mA/cm2, and H2O2 production rates as high as ~202 mg/h/cm2 could be obtained. Long-term stability test showed that the GDE maintained high ACEs (>85%) and low energy consumption (<10 kWh/kg H2O2) for H2O2 production for 42 d (~1000 h). However, the ACEs then decreased to ~70% in the following 4 days because water flooding of GDE pores considerably impeded oxygen transport at the late stage of the trial. Based on an electrode lifetime of 46 days, the overall cost for H2O2 production was estimated to be ~0.88 $/kg H2O2, including an electricity cost of 0.61 $/kg and an electrode capital cost of 0.27 $/kg. With a 9 cm2 GDE and 40 mA/cm2 current density, ~2–4 mg/L of H2O2 could be produced on site for the electro-peroxone treatment of a 1.2 m3/d groundwater flow, which considerably enhanced ibuprofen abatement compared with ozonation alone (~43%–59% vs. 7%). These findings suggest that electrochemical H2O2 production with GDEs holds great promise for the development of compact treatment technologies for decentralized water treatment at a household and community level.

Graphical abstract

Keywords

Advanced oxidation process / Electro-peroxone / Gas diffusion electrode / Hydrogen peroxide / Oxygen reduction

Cite this article

Download citation ▾
Yang Li, Yixin Zhang, Guangshen Xia, Juhong Zhan, Gang Yu, Yujue Wang. Evaluation of the technoeconomic feasibility of electrochemical hydrogen peroxide production for decentralized water treatment. Front. Environ. Sci. Eng., 2021, 15(1): 1 DOI:10.1007/s11783-020-1293-2

登录浏览全文

4963

注册一个新账户 忘记密码

References

[1]

Alcaide F, Álvarez G, Guelfi D R V, Brillas E, Sirés I (2020). A stable CoSP/MWCNTs air-diffusion cathode for the photoelectro-Fenton degradation of organic pollutants at pre-pilot scale. Chemical Engineering Journal, 379: 122417

[2]

Assumpção M H M T, De Souza R F B, Rascio D C, Silva J C M, Calegaro M L, Gaubeur I, Paixao T R L C, Hammer P, Lanza M R V, Santos M C (2011). A comparative study of the electrogeneration of hydrogen peroxide using Vulcan and Printex carbon supports. Carbon, 49(8): 2842–2851

[3]

Barazesh J M, Hennebel T, Jasper J T, Sedlak D L (2015). Modular advanced oxidation process enabled by cathodic hydrogen peroxide production. Environmental Science & Technology, 49(12): 7391–7399

[4]

Bolton J R, Bircher K G, Tumas W, Tolman C A (2001). Figures-of-merit for the technical development and application of advanced oxidation technologies for both electric- and solar-driven systems- (IUPAC Technical Report). Pure and Applied Chemistry, 73(4): 627–637

[5]

Brillas E, Mur E, Casado J (1996). Iron(II) catalysis of the mineralization of aniline using a carbon-PTFE O-2-fed cathode. Journal of the Electrochemical Society, 143(3): L49–L53

[6]

Brillas E, Sires I, Oturan M A (2009). Electro-Fenton process and related electrochemical technologies based on Fenton’s reaction chemistry. Chemical Reviews, 109(12): 6570–6631

[7]

Campos-Martin J M, Blanco-Brieva G, Fierro J L (2006). Hydrogen peroxide synthesis: an outlook beyond the anthraquinone process. Angewandte Chemie International Edition in English, 45(42): 6962–6984

[8]

Chaplin B P (2019). The prospect of electrochemical technologies advancing worldwide water treatment. Accounts of Chemical Research, 52(3): 596–604

[9]

Chen Z, Chen S, Siahrostami S, Chakthranont P, Hahn C, Nordlund D, Dimosthenis S, Nørskov J K, Bao Z, Jaramillo T F (2017). Development of a reactor with carbon catalysts for modular-scale, low-cost electrochemical generation of H2O2. Reaction Chemistry & Engineering, 2(2): 239–245

[10]

Ciriminna R, Albanese L, Meneguzzo F, Pagliaro M (2016). Hydrogen peroxide: A Key chemical for today’s sustainable development. ChemSusChem, 9(24): 3374–3381

[11]

Frangos P, Shen W H, Wang H J, Li X, Yu G, Deng S B, Huang J, Wang B, Wang Y J (2016). Improvement of the degradation of pesticide deethylatrazine by combining UV photolysis with electrochemical generation of hydrogen peroxide. Chemical Engineering Journal, 291: 215–224

[12]

Huber M M, Canonica S, Park G Y, Von Gunten U (2003). Oxidation of pharmaceuticals during ozonation and advanced oxidation processes. Environmental Science & Technology, 37(5): 1016–1024

[13]

Lin S, Lu Y, Ye B, Zeng C, Liu G, Li J, Luo H, Zhang R (2020). Pesticide wastewater treatment using the combination of the microbial electrolysis desalination and chemical-production cell and Fenton process. Frontiers of Environmental Science & Engineering, 14(1): 12

[14]

Lu S, Wang N, Wang C (2018a). Oxidation and biotoxicity assessment of microcystin-LR using different AOPs based on UV, O3 and H2O2. Frontiers of Environmental Science & Engineering, 12(3): 12

[15]

Lu Y B, Liu G L, Luo H P, Zhang R D (2017). Efficient in-situ production of hydrogen peroxide using a novel stacked electrosynthesis reactor. Electrochimica Acta, 248: 29–36

[16]

Lu Z, Chen G, Siahrostami S, Chen Z, Liu K, Xie J, Liao L, Wu T, Lin D, Liu Y, Jaramillo T F, Nørskov J K, Cui Y (2018b). High-efficiency oxygen reduction to hydrogen peroxide catalysed by oxidized carbon materials. Nature Catalysis, 1(2): 156–162

[17]

Oturan M A, Aaron J J, Oturan N, Pinson J (1999). Degradation of chlorophenoxyacid herbicides in aqueous media, using a novel electrochemical method. Pesticide Science, 55(5): 558–562

[18]

Paz E C, Aveiro L R, Pinheiro V S, Souza F M, Lima V B, Silva F L, Hammer P, Lanza M R V, Santos M C (2018). Evaluation of H2O2 electrogeneration and decolorization of Orange II azo dye using tungsten oxide nanoparticle-modified carbon. Applied Catalysis B: Environmental, 232: 436–445

[19]

Pérez J F, Llanos J, Sáez C, López C, Cañizares P, Rodrigo M A (2019). Towards the scale up of a pressurized-jet microfluidic flow-through reactor for cost-effective electro-generation of H2O2. Journal of Cleaner Production, 211: 1259–1267

[20]

Plakas K V, Sklari S D, Yiankakis D A, Sideropoulos G T, Zaspalis V T, Karabelas A J (2016). Removal of organic micropollutants from drinking water by a novel electro-Fenton filter: Pilot-scale studies. Water Research, 91: 183–194

[21]

Qiang Z, Chang J H, Huang C P (2002). Electrochemical generation of hydrogen peroxide from dissolved oxygen in acidic solutions. Water Research, 36(1): 85–94

[22]

Rezaei M, Warsinger D M, Lienhard V J H, Duke M C, Matsuura T, Samhaber W M (2018). Wetting phenomena in membrane distillation: Mechanisms, reversal, and prevention. Water Research, 139: 329–352

[23]

Salmerón I, Plakas K V, Sirés I, Oller I, Maldonado M I, Karabelas A J, Malato S (2018). Optimization of electrocatalytic H2O2 production at pilot plant scale for solar-assisted water treatment. Applied Catalysis B: Environmental, 242: 327–336

[24]

Sellers R M (1980). Spectrophotometric determination of hydrogen peroxide using potassium titanium(IV) oxalate. Analyst (London), 105(1255): 950–954

[25]

Sheng Y P, Zhao Y, Wang X L, Wang R, Tang T (2014). Electrogeneration of H2O2 on a composite acetylene black-PTFE cathode consisting of a sheet active core and a dampproof coating. Electrochimica Acta, 133: 414–421

[26]

Stoerzinger K A, Risch M, Han B H, Shao-Horn Y (2015). Recent insights into manganese oxides in catalyzing oxygen reduction kinetics. ACS Catalysis, 5(10): 6021–6031

[27]

Tang C, Wang H F, Zhang Q (2018). Multiscale principles to boost reactivity in gas-involving energy electrocatalysis. Accounts of Chemical Research, 51(4): 881–889

[28]

Turkay O, Barisci S, Ozturk B, Ozturk H, Dimoglo A (2017a). Electro-peroxone treatment of phenol: process comparison, the effect of operational parameters and degradation mechanism. Journal of the Electrochemical Society, 164(9): E180–E186

[29]

Turkay O, Ersoy Z G, Barisci S (2017b). Review—the application of an electro-peroxone process in water and wastewater treatment. Journal of the Electrochemical Society, 164(6): E94–E102

[30]

USEIA (2016). Annual Electric Sales, Revenue, and Average Price. Washington: U.S. Energy Information Administration

[31]

Valim R B, Reis R M, Castro P S, Lima A S, Rocha R S, Bertotti M, Lanza M R V (2013). Electrogeneration of hydrogen peroxide in gas diffusion electrodes modified with tert-butyl-anthraquinone on carbon black support. Carbon, 61: 236–244

[32]

von Gunten U (2018). Oxidation processes in water treatment: are we on track? Environmental Science & Technology, 52(9): 5062–5075

[33]

von Sonntag C, von Gunten U (2012). Chemistry of Ozone in Water and Wastewater Treatment: From Basic Principles to Applications. London: IWA Publishing

[34]

Wang H, Yuan S, Zhan J, Wang Y, Yu G, Deng S, Huang J, Wang B (2015). Mechanisms of enhanced total organic carbon elimination from oxalic acid solutions by electro-peroxone process. Water Research, 80: 20–29

[35]

Wang H, Zhan J, Yao W, Wang B, Deng S, Huang J, Yu G, Wang Y (2018a). Comparison of pharmaceutical abatement in various water matrices by conventional ozonation, peroxone (O3/H2O2), and an electro-peroxone process. Water Research, 130: 127–138

[36]

Wang Y, Li X, Zhen L, Zhang H, Zhang Y, Wang C (2012). Electro-Fenton treatment of concentrates generated in nanofiltration of biologically pretreated landfill leachate. Journal of Hazardous Materials, 229–230: 115–121

[37]

Wang Y, Yu G, Deng S, Huang J, Wang B (2018b). The electro-peroxone process for the abatement of emerging contaminants: Mechanisms, recent advances, and prospects. Chemosphere, 208: 640–654

[38]

Wang Y, Zhou W, Gao J, Ding Y, Kou K (2019). Oxidative modification of graphite felts for efficient H2O2 electrogeneration: Enhancement mechanism and long-term stability. Journal of Electroanalytical Chemistry, 833: 258–268

[39]

Warsinger D M, Swaminathan J, Guillen-Burrieza E, Arafat H A, Lienhard V J H (2015). Scaling and fouling in membrane distillation for desalination applications: A review. Desalination, 356: 294–313

[40]

WHO (2011). Guidelines for Drinking-Water Quality, 4th ed. Geneva: World Health Organization, 324

[41]

Xia G, Wang H, Zhan J, Yin X, Wu X, Yu G, Wang Y, Wu M (2020). Evaluation of the stability of polyacrylonitrile-based carbon fiber electrode for hydrogen peroxide production and phenol mineralization during electro-peroxone process. Chemical Engineering Journal, 396: 125291

[42]

Xia G, Wang Y, Wang B, Huang J, Deng S, Yu G (2017). The competition between cathodic oxygen and ozone reduction and its role in dictating the reaction mechanisms of an electro-peroxone process. Water Research, 118: 26–38

[43]

Yang S, Verdaguer-Casadevall A, Arnarson L, Silvioli L, Čolić V, Frydendal R, Rossmeisl J, Chorkendorff I, Stephens I E L (2018). Toward the decentralized electrochemical production of H2O2: a focus on the catalysis. ACS Catalysis, 8(5): 4064–4081

[44]

Yao W, Ur Rehman S W, Wang H, Yang H, Yu G, Wang Y (2018). Pilot-scale evaluation of micropollutant abatements by conventional ozonation, UV/O3, and an electro-peroxone process. Water Research, 138: 106–117

[45]

Yu X M, Zhou M H, Ren G B, Ma L (2015). A novel dual gas diffusion electrodes system for efficient hydrogen peroxide generation used in electro-Fenton. Chemical Engineering Journal, 263: 92–100

[46]

Yuan S, Li Z X, Wang Y J (2013). Effective degradation of methylene blue by a novel electrochemically driven process. Electrochemistry Communications, 29: 48–51

[47]

Zhang H, Chen S, Zhang H G, Fan X F, Cao C, Yu H T, Quan X (2019). Carbon nanotubes-incorporated MIL-88B-Fe as highly efficient Fenton-like catalyst for degradation of organic pollutants. Frontiers of Environmental Science & Engineering, 13(2): 18

[48]

Zhang X K, Zhou Y, Zhao C, Sun Z H, Zhang Z G, Mirza Z A, Saylor G, Zhai J, Zheng H L (2016). Electric field induced activated carbon fiber (ACF) cathode transition from an initiator/a promoter into an electrocatalyst in ozonation process. Chemical Engineering Journal, 304: 129–133

[49]

Zhou W, Meng X, Gao J, Alshawabkeh A N (2019). Hydrogen peroxide generation from O2 electroreduction for environmental remediation: A state-of-the-art review. Chemosphere, 225: 588–607

RIGHTS & PERMISSIONS

Higher Education Press

AI Summary AI Mindmap
PDF (1574KB)

Supplementary files

FSE-20066-OF-LY_suppl_1

4211

Accesses

0

Citation

Detail

Sections
Recommended

AI思维导图

/