ORALS
SESSION: BatteryFriAM-R11
| 6th Intl. Symp. on Sustainable Secondary Battery Manufacturing and Recycling |
Fri Oct, 25 2019 / Room: Coralino | |
Session Chairs: Katerina Aifantis; Rumen Tomov; Session Monitor: TBA |
12:35: [BatteryFriAM04]
Novel Carbon - Ultrafine Silicon Composite Anode for High-Performance Lithium-Ion Batteries Dmitry
Yarmolich
1 ; Dzianis
Yarmolich
2 ; Yaroslav
Odarchenko
3 ; Carmen
Murphy
4 ; Enrico
Petrucco
4 ;
Vasant
Kumar5 ;
Rumen
Tomov5 ;
1Plasma App Ltd, OX11 0QX, United Kingdom;
2Plasma App Ltd, Oxford , OX11 0QX, United Kingdom;
3Plasma App Ltd, Oxford OX11 0QX, United Kingdom;
4Johnson Matthey Battery Materials, Reading RG4 9NH, United Kingdom;
5University of Cambridge, Cambridge, United Kingdom;
Paper Id: 352
[Abstract] Silicon (Si) has been widely considered as potential high capacity anode material in Li-ion batteries due to its desirable properties: (i) high theoretical specific capacity (1672 mA h g-1), (ii) nontoxicity and (iii) low cost and natural abundance [1]. Despite its favourable comparison to commercial graphite anodes (theoretical capacity of 372 mA h g-1), the implementation of bulk Si anode has been hindered by the large volume change during the charging and discharging cycle (~ 300%). Such structural instability results in loss of contact with the other electrode constituents and self-destruction [2]. Another adverse feature is the limited Li<sup>+</sup> ion diffusivity and electronic conductivity of bulk Si at room temperature.
A scalable method of producing carbon (ultrafine silicon composite electrode) was developed using the Virtual Cathode Deposition technique [3]. As-deposited coatings contained silicon nano-crystallites encapsulated in a novel polymorph of mesoporous disordered carbon matrix. The architecture of the electrode offers close-order integration of both materials ensuring fast Li<sup>+</sup> ion diffusivity and mixed-(ionic/electronic) conductivity as well as alleviating Si volume change during cycling. The composite carbon polymorph-silicon anode tested versus Li displayed a first cycle specific capacity of more than 2000 mAh g<sup>-1</sup> retaining in the following cycles ~1200 mAh g<sup>-1</sup> at a 0.1C rate. The good cyclability (over 80 cycles) demonstrated the effectiveness of such Si - carbon encapsulation, addressing the instability issues of Si-based anodes.
References:
[1] P. G. Bruce, S. A. Freunberger, L. J. Hardwick and J. M. Tarascon, Nat. Mater., 2012, 11, 19–29.
[2] Li B, Xiao Q, Luo Y (2018) A modified synthesis process of three dimensional sulfur/graphene aerogel as binder-free cathode for lithium-sulfur batteries. Mater Des 153:9–14
[3] D. Yarmolich, D. Virtual cathode deposition (vcd) for thin film manufacturing WO2016042530A1. (2015).
13:00 LUNCH
SESSION: BatteryFriPM1-R11
| 6th Intl. Symp. on Sustainable Secondary Battery Manufacturing and Recycling |
Fri Oct, 25 2019 / Room: Coralino | |
Session Chairs: Guoran Li; Claudio Capiglia; Session Monitor: TBA |
14:00: [BatteryFriPM105]
Feasibility of a Physical Vapor Deposition technology for battery electrode manufacturing Dmitry
Yarmolich1 ;
Rumen
Tomov2 ;
Vasant
Kumar2 ; Carmen
Murphy
3 ; Yaroslav
Odarchenko
4 ; Dzianis
Yarmolich
5 ; Enrico
Petrucco
3 ;
1Plasma App Ltd, OX11 0QX, United Kingdom;
2University of Cambridge, Cambridge, United Kingdom;
3Johnson Matthey Battery Materials, Reading RG4 9NH, United Kingdom;
4Plasma App Ltd, Oxford OX11 0QX, United Kingdom;
5Plasma App Ltd, Oxford , OX11 0QX, United Kingdom;
Paper Id: 504
[Abstract] The method of physical vapor deposition has been tested for the manufacture of electric vehicle lithium-ion battery anodes. The anode was fabricated using Virtual Cathode Deposition1 (VCD) which enables direct deposition of 20 μm thick carbon active material onto a 25 μm polypropylene separator, followed by deposition of a 2 μm copper current collector. Carbon polymorphism2 induced by the deposition process is responsible for active material high gravimetric and volumetric capacity allowing anode areal capacity up to 4.2 mAh/cm2 at the 0.1 C charge rate. The PVD process increases the purity of active materials and quality control compared to the state-of-the-art wet chemical3 method. Currently, the production of a 24 kWh Nissan Leaf’s battery pack requires about 25 MWh, more than 80% of which is spent on drying the electrodes and dry room conditioning. VCD eliminates use of solvents that saves the energy for electrode drying and increase the environmental safety of battery production.
References:
1. Yarmolich, D. Patent No. WO2016042530A1 (September 2014).
2. Zhao, C. X., Niu, Ch. Y., Qin, Z-J., Ren, X. Y., Wang, J-T., Cho J.H. and Jia, Y. H18Carbon: A New Metallic Phase with sp2-sp3 Hybridized Bonding Network. Sci. Rep. 6, 1–9 (2016).
3. A. Sakti , J. J. Michalek, E. R.H. Fuchs, Jay F. Whitacre., A techno-economic analysis and optimization of Li-ion batteries for light-duty passenger vehicle electrification. Journal of Power Sources 273 (2015)
4. C. Yuan, Ye. Deng, T. Li, F. Yang, Manufacturing energy analysis of lithium ion battery pack for electric vehicles, CIRP Annals - Manufacturing Technology 66 (2017)
SESSION: BatteryFriPM2-R11
| 6th Intl. Symp. on Sustainable Secondary Battery Manufacturing and Recycling |
Fri Oct, 25 2019 / Room: Coralino | |
Session Chairs: Katsuya Teshima; Deise Menezes Santos; Session Monitor: TBA |
15:55: [BatteryFriPM209]
Production of Ultra-Pure Lead Citrate from Spent Lead-Acid Battery Paste using a Cost-Effective, Eco-Friendly Process Vimalnath
Selvaraj1 ; Marcel
Yiao
1 ; Robert
Liu
2 ;
Rumen
Tomov1 ;
Vasant
Kumar1 ; Peter
Knight
1 ; Steve
Andrew
2 ; Spencer
Lowe
2 ;
Athan
Fox3 ;
Miles
Freeman2 ; Johdie
Harris
2 ;
1University of Cambridge, Cambridge, United Kingdom;
2Aurelius Environmental, Dudley, United Kingdom;
3Aurelius Environmental, Tipton, United Kingdom;
Paper Id: 415
[Abstract] Abstract
The recovery of Pb from the spent lead-acid battery paste is achieved conventionally through pyrometallurgical processes. This process requires relatively high temperature (~1,100 °C) for the decomposition of PbSO4 which is a dominant compound in the paste along with PbO2, PbO, metallic Pb and other impurities. The high-temperature pyrometallurgical process releases SO2 gas and Pb particulates into the environment, raising serious environmental concerns. The hydro-electro metallurgical process, which has been developed as an alternative, also consumes high energy and uses toxic acids like HBF4 or H2SiF6. The need for an eco-friendly and cost-effective recycling process for the recovery of spent battery paste [1,2,3,4], is not only critical but also very timely. Indeed, the market size of secondary lead-acid batteries is forecasted to reach over $95 billion USD by 2026 [5]. Within this market, the recycling of lead-acid batteries is a revenue stream worth around $14-16 billion USD by 2025 [6].
In this paper, we present our work towards a fully hydrometallurgical, eco-friendly and cost-effective process. The recovery of Pb is achieved through the synthesis of ultrapure lead-citrate, which is obtained directly from spent lead-acid battery paste via desulphurisation and treatment with organic acids. Unlike previous iterations of this process, we have optimised the conditions to achieve production of ultra-pure lead-citrate, 99.99%, with minimum consumption of reagents. This paper shows how it is possible to minimise production costs for the recycled lead compounds to the extent that the process is as cost-effective, if not superior economically, when compared to the incumbent technology. The scalability and economic improvement of the latest iteration of this now-patented hydrometallurgical process greatly facilitate the globalisation of this innovative technology.
Keywords
Lead, battery, recycling, lead citrate, hydrometallurgy, organic acids
References:
References
[1] Sonmez, M. S., and R. V. Kumar, Hydrometallurgy 95.1-2 (2009) 53-60.
[2] Sonmez, M. S., and R. V. Kumar, Hydrometallurgy 95.1-2 (2009) 82-86.
[3] Yang, Jiakuan, Ramachandran Vasant Kumar, and Deepak P. Singh, Journal of Chemical Technology & Biotechnology 87.10 (2012) 1480-1488.
[4] Zhu, X., He, X., Yang, J., Gao, L., Liu, J., Yang, D., Sun, X., Zhang, W., Wang, Q. and Kumar, R.V, Journal of Hazardous Materials 250 (2013) 387-396.
[5] https://www.reportsanddata.com (report ID RND_00104)
[6] https://www.cambridgeindependent.co.uk/business/cambridge-battery-recycling-technology-set-to-disrupt-global-market-9052189/