Jian-Guang Yang
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Research Subjects
Jian-Guang Yang has a total of 24 co-authors. Here are the top co-authors by number of shared publications:
Chao-Bo Tang
Central South University
5 shared publicationsMo-Tang Tang
Central South University
3 shared publicationsSheng-Hai Yang
Central South University
3 shared publicationsChao‐Bo Tang
2 shared publicationsJing He
2 shared publicationsLei Jie
Central South University
2 shared publications
Latest Publications
- 5 February 2017
- Published by Springer Nature
- p. 285-301
The Recovery of Bismuth from Bismuthinite Concentrate Through Membrane Electrolysis
- 5 February 2017
- Published by Springer Nature
- p. 285-301
The Recovery of Bismuth from Bismuthinite Concentrate Through Membrane Electrolysis
- 6 September 2016
- Published by Wiley in Journal of Chemical Technology & Biotechnology
- Vol. 92 (4) , 861-867
Electrochemical mechanism of tin membrane electro‐deposition in chloride solutions
BACKGROUND: A new membrane electro‐deposition based process for tin recovery from stannous solid waste was introduced. Linear sweep voltammetry (LSV), cyclic voltammetry (CV) and chronoamperometry (CHR) was applied to investigate the electrodeposition of tin(II) from a stannous chloride acid electrolyte containing an amine non‐ionic surfactant by using a membrane cell.RESULTS: Electrochemical mechanism analysis results showed that 0.3% vol. amine non‐ionic surfactant facilitated ions diffusion by increasing the diffusion coefficient from 8.32E‐12 m2 s−1 to 2.85E‐11 m2 s−1, and inhibited tin(II) ions reduction as well as tin nucleation and hydrogen evolution. The applied ionic membrane did not hinder tin electrodeposition, while tin(II) ions reduction and hydrogen evolution was weakened with increasing HCl concentration from 1.5 to 4.5 mol L−1 and Sn2+ concentration increased from 20 to 80 g L−1.CONCLUSIONS: The tin(II) reduction process is proved to be irreversible and diffusion‐controlled, while the nucleation and growth of tin was involved in the process of diffusion for the proton reduction occuring in parallel with tin electrodeposition, and the process follows the mechanism of three‐dimensional instantaneous nucleation and subsequent grain growth limited by diffusion. © 2016 Society of Chemical Industry
- 6 September 2016
- Published by Wiley in Journal of Chemical Technology & Biotechnology
- Vol. 92 (4) , 861-867
Electrochemical mechanism of tin membrane electro‐deposition in chloride solutions
BACKGROUND: A new membrane electro‐deposition based process for tin recovery from stannous solid waste was introduced. Linear sweep voltammetry (LSV), cyclic voltammetry (CV) and chronoamperometry (CHR) was applied to investigate the electrodeposition of tin(II) from a stannous chloride acid electrolyte containing an amine non‐ionic surfactant by using a membrane cell.RESULTS: Electrochemical mechanism analysis results showed that 0.3% vol. amine non‐ionic surfactant facilitated ions diffusion by increasing the diffusion coefficient from 8.32E‐12 m2 s−1 to 2.85E‐11 m2 s−1, and inhibited tin(II) ions reduction as well as tin nucleation and hydrogen evolution. The applied ionic membrane did not hinder tin electrodeposition, while tin(II) ions reduction and hydrogen evolution was weakened with increasing HCl concentration from 1.5 to 4.5 mol L−1 and Sn2+ concentration increased from 20 to 80 g L−1.CONCLUSIONS: The tin(II) reduction process is proved to be irreversible and diffusion‐controlled, while the nucleation and growth of tin was involved in the process of diffusion for the proton reduction occuring in parallel with tin electrodeposition, and the process follows the mechanism of three‐dimensional instantaneous nucleation and subsequent grain growth limited by diffusion. © 2016 Society of Chemical Industry
- 1 March 2016
- Published by Elsevier in Journal of Hazardous Materials
- Vol. 304, 409-416
A new membrane electro-deposition based process for tin recovery from waste printed circuit boards
- 1 March 2016
- Published by Elsevier in Journal of Hazardous Materials
- Vol. 304, 409-416
A new membrane electro-deposition based process for tin recovery from waste printed circuit boards
- 22 November 2014
- Published by Springer Nature in JOM
- Vol. 67 (2) , 477-483
Separation of Silver from a Zinc Sulfide Concentrate by a Co-smelting Process
- 22 November 2014
- Published by Springer Nature in JOM
- Vol. 67 (2) , 477-483
Separation of Silver from a Zinc Sulfide Concentrate by a Co-smelting Process
- 12 February 2013
- Published by Springer Nature in Metallurgical and Materials Transactions B
- Vol. 44 (2) , 479-481
Erratum to: The Membrane Electrowinning Separation of Antimony from a Stibnite Concentrate
- 12 February 2013
- Published by Springer Nature in Metallurgical and Materials Transactions B
- Vol. 44 (2) , 479-481
Erratum to: The Membrane Electrowinning Separation of Antimony from a Stibnite Concentrate
- 28 February 2011
- Published by Wiley
- p. 749-756
Separation of Antimony from a Stibnite Concentrate through a Low‐Temperature Smelting Process to Eliminate SO2emission
- 28 February 2011
- Published by Wiley
- p. 749-756
Separation of Antimony from a Stibnite Concentrate through a Low‐Temperature Smelting Process to Eliminate SO2emission
- 28 February 2011
- Published by Wiley
- p. 741-748
Electrosynthesis, Characterization, and Thermal Property Analysis of Pentakis (Diethylamido) Tantalum
- 28 February 2011
- Published by Wiley
- p. 741-748
Electrosynthesis, Characterization, and Thermal Property Analysis of Pentakis (Diethylamido) Tantalum
- 23 November 2010
- Published by Springer Nature in Metallurgical and Materials Transactions B
- Vol. 42 (1) , 30-36
Separation of Antimony from a Stibnite Concentrate Through a Low-Temperature Smelting Process to Eliminate SO2 Emission
- 23 November 2010
- Published by Springer Nature in Metallurgical and Materials Transactions B
- Vol. 42 (1) , 30-36
Separation of Antimony from a Stibnite Concentrate Through a Low-Temperature Smelting Process to Eliminate SO2 Emission
- 1 October 2010
- Vol. 101 (19) , 7653-7
Heavy metal removal and crude bio-oil upgrading from Sedum plumbizincicola harvest using hydrothermal upgrading process.
The main aim of this study was to separate heavy metals and yield crude bio-oil from a heavy metals hyperaccumulator harvest, Sedum plumbizincicola, through hydrothermal upgrading process. Parameters such as granularity, temperature, pressure, and duration were examined for their effect on the removal efficiency of heavy metals and upgrading efficacy of crude bio-oil. Maximum heavy metal removal efficiency of >99% and crude bio-oil upgrading efficiency of >63% were attained with an 18 mesh (1 mm) granularity, and 22.1 MPa at 370 degrees C in the presence of 10 mg/L additives for 60 s. Under these optimized conditions, an oil phase (mostly composed of phenolic hydrocarbons and derivatives), a water phase raffinate containing Zn2+ (0.39 g/L), Pb2+ (0.10 g/L), Cu2+ (0.16 g/L), and a solid phase (the hydrothermal upgrading residue, which completely satisfies the limit set by China legislation related to biosolids disposal, were obtained).
- 1 October 2010
- Vol. 101 (19) , 7653-7
Heavy metal removal and crude bio-oil upgrading from Sedum plumbizincicola harvest using hydrothermal upgrading process.
The main aim of this study was to separate heavy metals and yield crude bio-oil from a heavy metals hyperaccumulator harvest, Sedum plumbizincicola, through hydrothermal upgrading process. Parameters such as granularity, temperature, pressure, and duration were examined for their effect on the removal efficiency of heavy metals and upgrading efficacy of crude bio-oil. Maximum heavy metal removal efficiency of >99% and crude bio-oil upgrading efficiency of >63% were attained with an 18 mesh (1 mm) granularity, and 22.1 MPa at 370 degrees C in the presence of 10 mg/L additives for 60 s. Under these optimized conditions, an oil phase (mostly composed of phenolic hydrocarbons and derivatives), a water phase raffinate containing Zn2+ (0.39 g/L), Pb2+ (0.10 g/L), Cu2+ (0.16 g/L), and a solid phase (the hydrothermal upgrading residue, which completely satisfies the limit set by China legislation related to biosolids disposal, were obtained).