Development of an Aspen Plus® Model for the Process of Hydrogen Production by Black Liquor Electrolysis

被引:2
作者
Goncalves, Jose R. M. [1 ,2 ]
Cecilio, Duarte M. [2 ]
Oliveira, Raisa C. P. [1 ,2 ]
Mateus, Maria M. [2 ]
Santos, Diogo M. F. [1 ]
机构
[1] Univ Lisbon, Ctr Phys & Engn Adv Mat, Inst Super Tecn, Lab Phys Mat & Emerging Technol,Chem Engn Dept, P-1049001 Lisbon, Portugal
[2] Univ Lisbon, Ctr Nat Resources & Environm, Inst Super Tecn, Chem Engn Dept, P-1049001 Lisbon, Portugal
来源
SYMMETRY-BASEL | 2022年 / 14卷 / 08期
关键词
black liquor; electrolysis; lignin; hydrogen; modeling; Aspen Plus (R); Aspen Custom Modeler; LIGNIN; SIMULATION;
D O I
10.3390/sym14081676
中图分类号
O [数理科学和化学]; P [天文学、地球科学]; Q [生物科学]; N [自然科学总论];
学科分类号
07 ; 0710 ; 09 ;
摘要
The electrolysis of black liquor (BL) has emerged as a new form to valorize this byproduct from the pulp and paper industry. BL electrolysis produces a green fuel, hydrogen, and lignin, a high added-value compound. In opposition to water electrolysis, a symmetric process with two different gases produced at the electrodes, hydrogen and oxygen, BL electrolysis is seen as an asymmetric process, as hydrogen is the only gas generated (at the cathode), while solid lignin is electrodeposited at the anode. The present work intended to develop a model in Aspen Plus (R) to simulate BL electrolysis and consequently evaluate the performance of the BL electrolyzer. Aspen Plus (R) does not include a package for electrolyzers, so it was necessary to use the Aspen Custom Modeler (ACM) tool. The model developed in ACM is valid for the following conditions: nickel electrodes with 2 cm interelectrode distance, cell voltage between 1.5 V and 2.0 V, and temperatures between 25 and 35 degrees C for batch operation and 25 and 65 degrees C for continuous operation. Sensitivity analysis demonstrated that the optimum working temperature for batch operation is 35 degrees C, whereas it is 45 degrees C for continuous operation. An economic analysis was carried out, calculating the real gross profit (RGP) for the process and the electricity cost. A 2 kW electrolyzer with 80 cells and an active area of 0.3 m(2) was simulated. For the electrolyzer in batch operation, RGP values of 1056 euro/year and 1867 euro/year for the worst and the best scenario were obtained, respectively, and the electricity cost was 1431 euro/year. For continuous operation, the RGP values were 2064 euro/year and 3648 euro/year for the worst and best scenario, respectively, and 2967 euro/year for the electricity costs.
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页数:19
相关论文
共 31 条
  • [1] Anderson ZR, 2019, ANTIPODE BOOK SER, P83
  • [2] Barrett A, EUROPEAN COMMISSION
  • [3] Belo I, 2018, THESIS I SUPERIOR TE
  • [4] Development of a Black Liquor Electrolyzer for Lignin Extraction
    Belo, I. C.
    Oliveira, R. C. P.
    Mateus, M. M.
    Bordado, J. C. M.
    Pinto, P. C. R.
    Santos, D. M. F.
    [J]. ELECTROCHEMICAL ENGINEERING GENERAL SESSION -AND- CHARACTERIZATION OF ELECTROCHEMICAL REACTORS: FLUID DYNAMICS AND CURRENT DISTRIBUTION, 2018, 86 (04): : 3 - 9
  • [5] Bontempelli G, 2016, Reference Module in Chemistry, Molecular Sciences and Chemical Engineering, P1
  • [6] Emission and odour control in Kraft pulp mills
    Bordado, JCM
    Gomes, JFP
    [J]. JOURNAL OF CLEANER PRODUCTION, 2003, 11 (07) : 797 - 801
  • [7] Towards a sustainable technology for H2 production: Direct lignin electrolysis in a continuous-flow Polymer Electrolyte Membrane reactor
    Caravaca, Angel
    Eunice Garcia-Lorefice, Wendy
    Gil, Sonia
    de Lucas-Consuegra, Antonio
    Vernoux, Philippe
    [J]. ELECTROCHEMISTRY COMMUNICATIONS, 2019, 100 : 43 - 47
  • [8] Electrochemical hydrogen production from biomass
    Dolle, Cyrielle
    Neha, Neha
    Coutanceau, Christophe
    [J]. CURRENT OPINION IN ELECTROCHEMISTRY, 2022, 31
  • [9] Solar Thermochemical Hydrogen Production in the USA
    Falter, Christoph
    Sizmann, Andreas
    [J]. SUSTAINABILITY, 2021, 13 (14)
  • [10] Towards the Development of Syngas/Biomethane Electrolytic Production, Using Liquefied Biomass and Heterogeneous Catalyst
    Goncalves, Ana
    Puna, Jaime Filipe
    Guerra, Luis
    Rodrigues, Jose Campos
    Gomes, Joao Fernando
    Santos, Maria Teresa
    Alves, Diogo
    [J]. ENERGIES, 2019, 12 (19)