WO2003016593A2 - Hydrogen evolution inhibiting additives for zinc electrowinning - Google Patents

Hydrogen evolution inhibiting additives for zinc electrowinning Download PDF

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Publication number
WO2003016593A2
WO2003016593A2 PCT/CA2002/001250 CA0201250W WO03016593A2 WO 2003016593 A2 WO2003016593 A2 WO 2003016593A2 CA 0201250 W CA0201250 W CA 0201250W WO 03016593 A2 WO03016593 A2 WO 03016593A2
Authority
WO
WIPO (PCT)
Prior art keywords
zinc
cpc
zinc electrowinning
electrowinning
current efficiency
Prior art date
Application number
PCT/CA2002/001250
Other languages
French (fr)
Other versions
WO2003016593A3 (en
Inventor
Elod Lajos Gyenge
Joey Chung-Yen Jung
Klaus Heinrich Oehr
Steven Splinter
Colin W. Oloman
Original Assignee
Magpower Systems Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority to CA002457071A priority Critical patent/CA2457071C/en
Application filed by Magpower Systems Inc. filed Critical Magpower Systems Inc.
Priority to JP2003520877A priority patent/JP2004537653A/en
Priority to BR0211933-1A priority patent/BR0211933A/en
Priority to EP02754027A priority patent/EP1417357B1/en
Priority to KR1020047002247A priority patent/KR100599993B1/en
Priority to AU2002322888A priority patent/AU2002322888B2/en
Priority to DE60203301T priority patent/DE60203301T2/en
Priority to MXPA04001459A priority patent/MXPA04001459A/en
Priority to US10/486,711 priority patent/US20050011769A1/en
Publication of WO2003016593A2 publication Critical patent/WO2003016593A2/en
Publication of WO2003016593A3 publication Critical patent/WO2003016593A3/en
Priority to NO20040651A priority patent/NO20040651L/en
Priority to HK05108025A priority patent/HK1075920A1/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C1/00Electrolytic production, recovery or refining of metals by electrolysis of solutions
    • C25C1/16Electrolytic production, recovery or refining of metals by electrolysis of solutions of zinc, cadmium or mercury

Definitions

  • the invention is related to additives for zinc
  • cetylpyridinium-based additives cetylpyridinium-based additives .
  • additives generally organic compounds, which selectively increase the hydrogen evolution overpotential .
  • Cetylpyridinium chloride (CPC) a cetylpyridinium salt
  • the CPC additive had the most significant influence in the presence of antimony or antimony + glue combination, where it
  • electrowinning electrolyte (liquor) were connected to a power
  • the anodes and cathodes were made of lead and aluminium, respectively.
  • composition zinc sulfate 28 - 34% by weight, magnesium sulfate
  • CPC cetylpyridinium chloride
  • Table 1 Effect of CPC on the current efficiency of zinc electrowinning in the electrolyte containing 0.04 mg/1 Sb (as Sb-tartrate) .
  • Table 3 Effect of CPC on the current efficiency of zinc electrowinning in the electrolyte containing 0.04 mg/1 Sb (as Sb-tartrate) + 10 mg/1 glue.
  • the cell voltage is another important figure of merit of
  • Table 5 Effect of CPC on the average cell voltage in 4 hour experiments with 0.04 mg/1 Sb and 10 mg/1 glue in the electrolyte.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electrolytic Production Of Metals (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Primary Cells (AREA)

Abstract

A cetylpyridinium salt, cetylpyridinium chloride (CPC) is used as a hydrogen evolution inhibitor (a current efficiency improver) in a commercial zinc electrowinning process. Zinc electrowinning compositions containing a) antimony and b) antimony and glue were tested. Adding CPC at a 0.05mM concentration to the electrowinning liquor resulted in increased current efficiency for both electrolytes.

Description

HYDROGEN EVOLUTION INHIBITING ADDITIVES FOR ZINC ELECTROWINNING
FIELD
• The invention is related to additives for zinc
electrowinning that inhibit hydrogen evolution and/or improve
current efficiency for zinc electrodeposition, specifically
cetylpyridinium-based additives .
BACKGROUND
Improving the energy efficiency of the zinc electrowinning
process by inhibition of the parasitic hydrogen evolution
reaction, which occurs in parallel with zinc deposition, is of
major technological and commercial interest. One way of
minimizing the cathodic hydrogen evolution is by the use of
additives, generally organic compounds, which selectively increase the hydrogen evolution overpotential . Mackinnon et al .
(Journal of Applied Electrochemistry, Volume 20, pages 728-736,
1990) and Scott et al. (Journal of Applied Electrochemistry,
Volume 18, pages 120-127, 1988) describe the use of animal glue
in combination with antimony to improve the current efficiency
for zinc electrowinning when compared to additive-free
electrolytes .
There is a need for improved additives that minimize hydrogen evolution during zinc electrowinning while providing
the same or improved performance over traditional additives .
Therefore, it is an object of this invention to provide
improved additives for zinc electrowinning that minimize
hydrogen evolution while providing similar or improved
performance over traditional additives .
SUMMARY
Cetylpyridinium chloride (CPC) , a cetylpyridinium salt, was
tested as an additive in a zinc electrowinning process in two
separate zinc electrowinning electrolyte compositions: 1) with
antimony and 2) with both antimony and glue.
The CPC additive had the most significant influence in the presence of antimony or antimony + glue combination, where it
increased the current efficiency by 23.2% and 7.6%,
respectively. Moreover, the presence of 0.05 mM CPC did not
increase the overall cell voltage.
DETAILED DESCRIPTION
Methods And Apparatus
Commercial beaker test cells containing a commercial
electrowinning electrolyte (liquor) were connected to a power
supply and placed in a 37 °C water bath. The anodes and cathodes were made of lead and aluminium, respectively. The laboratory
supplied MSDS sheet indicated for the electrolyte the following
composition: zinc sulfate 28 - 34% by weight, magnesium sulfate
9 - 15 g/1 (grams/litre) and manganese 1.5 - 2.5 g/1.
After allowing the temperature inside the test cells to
reach the desired value of 37 °C, a constant current of 0.045 A,
representing an electrowinning current density of 450
amperes/meter2, was applied for either 4 or 20 hours to a non-
agitated electrolyte. After completion of the experiment the
electrode assembly was removed from the glass beaker, rinsed
with distilled water and the cathode deposit carefully scraped
off and weighed with four digits precision using a digital
Mettler AE 100 analytical balance. The test cells were rinsed
between experiments with distilled water and acetone in order to
remove traces of the organic additives . Replicates were also
performed and the standard deviation was estimated.
The zinc electrodeposition current efficiency was
calculated based on Faraday's law:
C£(%)=— MOO (1)
where
CE - current efficiency for Zn electrodeposition (%) z - no. of electrons exchanged [=2] F - Faraday's number [=96485.3 C mol"1] md - amount of zinc deposit (g) /- applied current [=0.045 A] t - time (s)
Azn - atomic weight of zinc [=65.39].
The cetylpyridinium chloride (CPC) (e.g. Sigma-Aldrich,
U.S.) had the following structure:
Figure imgf000005_0001
Figure imgf000005_0002
Example 1
Zinc Electrowinning Liquor with antimony present
Antimony (Sb) in 0.04 mg/1 (milligrams/litre) concentration
was added as antimony - potassium tartrate to the zinc
electrowinning electrolyte. Both four and twenty hour runs were
performed. The experimental results of the four-hour runs are
summarized in Table 1.
Without the CPC additive present in the electrolyte, Sb had
a detrimental effect on the current efficiency, i.e. between 65.1% (cell no. 15) and 74.7% (cell no. 14). On average, the
current efficiency without the CPC additive present was 69.9%.
Adding CPC improved the current efficiency on average by 23.2%,
i.e. from 69.9% to 93.1%.
Table 1: Effect of CPC on the current efficiency of zinc electrowinning in the electrolyte containing 0.04 mg/1 Sb (as Sb-tartrate) .
Figure imgf000006_0001
CA
The effect of CPC inΛlonger-term (20 hours) experiment is
shown in Table 2. Without the CPC additive, the current
efficiency of cell no. 15 was only 36.6%, whilst with 0.05 mM
CPC present the zinc electrowinning current efficiency was
58.9%. Thus, with the CPC additive the current efficiency was
higher by 22.3%. Table 2: Effect of CPC on the zinc electrowinning current efficiency in 20 hour experiment with 0.04 mg/1 Sb in the electrolyte.
Figure imgf000007_0001
"5
Example 2
Zinc Electrowinning Liquor with both antimony and glue
Similar experiments to those in Example 1 were performed
with an electrolyte containing 0.04 mg/1 of Sb and 10 mg/1 of
10 glue (e.g. "pearl glue" supplied by Hudson Industries,
Johnstown, New York) . Both 4 and 20 hour runs were carried out,
The effect of the CPC additive on the zinc electrowinning .
current efficiency in the 4 hour runs is shown in Table 3.
15 The presence of glue minimizes to a certain extent the
negative effect of antimony, yielding current efficiencies
between 88.9% and 90%. However, adding 0.05 mM CPC brought
about additional increases of current efficiency, i.e. from
89.4% on average in the absence to 97% in the presence of CPC
20 (Table 3) . Table 3: Effect of CPC on the current efficiency of zinc electrowinning in the electrolyte containing 0.04 mg/1 Sb (as Sb-tartrate) + 10 mg/1 glue.
Figure imgf000008_0001
The 20 hour experiments (Table 4) showed that CPC in 0.05
mM concentration increased the current efficiency of cell no . 16
from 77.2% to 87.3%.
Table : Effect of CPC on the zinc electrowinning current efficiency in 20 hour experiment with 0.04 mg/1 Sb and 10 mg/1 glue in the electrolyte.
Figure imgf000008_0002
The cell voltage is another important figure of merit of
the electrowinning process. An increase in the cell voltage
represents an increase in the amount of energy required and, therefore, a less efficient electrowinning process. Table 5
shows that using 0.05 mM CPC in conjunction with Sb and glue did
not induce an increase of the cell voltage.
Table 5 : Effect of CPC on the average cell voltage in 4 hour experiments with 0.04 mg/1 Sb and 10 mg/1 glue in the electrolyte.
Figure imgf000009_0001
Accordingly, while this invention has been described with
reference to illustrative embodiments, this description is not
intended to be construed in a limiting sense. Various
modifications of the illustrative embodiments, as well as other
embodiments of the invention, will be apparent to persons
skilled in the art upon reference to this description. It is
therefore contemplated that the appended claims will cover any
such modifications or embodiments as fall within the scope of the invention.

Claims

WE CLAIM :
1. A method of improved zinc electrowinning, comprising : adding a cetylpyridinium salt additive to a zinc electrowinning electrolyte .
2 . A method according to claim 1, wherein said cetylpyridinium salt is a cetylpyridinium halide .
3 . A method according to claim 2 , wherein said cetylpyridinium halide is cetylpyridinium chloride .
4 . A method according to claim 3 , wherein said cetylpyridinium chloride is at 0 . 05 millimolar (mM) concentration in said zinc electrowinning liquor.
5. A method according to claim 1, wherein said zinc
electrowinning electrolyte contains zinc sulfate.
6. A method according to claim 1, wherein said zinc
electrowinning electrolyte contains antimony.
7. A method according to claim 1, wherein said zinc
electrowinning electrolyte contains glue.
8. A method according to claim 7 , wherein said glue is animal
glue.
9. A method according, to claim 8 , wherein said animal glue is
gelatin.
PCT/CA2002/001250 2001-08-14 2002-08-13 Hydrogen evolution inhibiting additives for zinc electrowinning WO2003016593A2 (en)

Priority Applications (11)

Application Number Priority Date Filing Date Title
AU2002322888A AU2002322888B2 (en) 2001-08-14 2002-08-13 Hydrogen evolution inhibiting additives for zinc electrowinning
JP2003520877A JP2004537653A (en) 2001-08-14 2002-08-13 Hydrogen evolution control additive for zinc electrowinning
BR0211933-1A BR0211933A (en) 2001-08-14 2002-08-13 Hydrogen Evolution Inhibition Additives for Zinc Electroproduction
EP02754027A EP1417357B1 (en) 2001-08-14 2002-08-13 Hydrogen evolution inhibiting additives for zinc electrowinning
KR1020047002247A KR100599993B1 (en) 2001-08-14 2002-08-13 Hydrogen evolution inhibiting additives for zinc electrowinning
CA002457071A CA2457071C (en) 2001-08-14 2002-08-13 Hydrogen evolution inhibiting additives for zinc electrowinning
DE60203301T DE60203301T2 (en) 2001-08-14 2002-08-13 ADDITIVES FOR PREVENTING HYDROGEN FORMATION IN THE ELECTROLYTIC OBTAINING OF ZINC
MXPA04001459A MXPA04001459A (en) 2001-08-14 2002-08-13 Hydrogen evolution inhibiting additives for zinc electrowinning.
US10/486,711 US20050011769A1 (en) 2001-08-14 2002-08-13 Hydrogen evolution inhibiting additives for zinc electrowinning
NO20040651A NO20040651L (en) 2001-08-14 2004-02-13 Hydrogen development inhibitory additives for zinc electroproduction.
HK05108025A HK1075920A1 (en) 2001-08-14 2005-09-14 Hydrogen evolution inhibiting additives for zinc electrowinning

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US31182501P 2001-08-14 2001-08-14
US60/311,825 2001-08-14

Publications (2)

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WO2003016593A2 true WO2003016593A2 (en) 2003-02-27
WO2003016593A3 WO2003016593A3 (en) 2003-10-09

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EP (1) EP1417357B1 (en)
JP (1) JP2004537653A (en)
KR (1) KR100599993B1 (en)
CN (1) CN100342061C (en)
AU (1) AU2002322888B2 (en)
BR (1) BR0211933A (en)
CA (1) CA2457071C (en)
DE (1) DE60203301T2 (en)
ES (1) ES2238586T3 (en)
HK (1) HK1075920A1 (en)
MX (1) MXPA04001459A (en)
NO (1) NO20040651L (en)
RU (1) RU2288299C2 (en)
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Publication number Priority date Publication date Assignee Title
CN100540748C (en) * 2006-06-15 2009-09-16 云南冶金集团总公司 Assembled gelatin additive
CN103993330A (en) * 2014-05-07 2014-08-20 成都理工大学 Zinc electrolysis technology of zinc ammonia complex aqueous solution
CN106676578B (en) * 2015-11-11 2018-09-28 沈阳有色金属研究院 A kind of new and effective joint additive of Zinc electrolysis
CN110512236B (en) * 2019-09-27 2021-05-04 中国科学院长春应用化学研究所 Combined additive and application thereof in zinc electrodeposition
CN115133159A (en) * 2022-09-01 2022-09-30 河南师范大学 Functional aqueous zinc ion battery electrolyte and preparation method and application thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4028199A (en) * 1974-08-05 1977-06-07 National Development Research Corporation Method of producing metal powder
WO2000039367A2 (en) * 1998-12-23 2000-07-06 Half Tone Limited Solution and process for the electrodeposition of gold and gold alloys
US6238542B1 (en) * 1998-09-15 2001-05-29 Thomas Helden Water soluble brighteners for zinc and zinc alloy electrolytes

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1064852A (en) * 1975-12-31 1979-10-23 Cominco Ltd. Method for evaluating a system for electrodeposition of metals
CA1111125A (en) * 1978-07-05 1981-10-20 Robert C. Kerby Method and apparatus for control of electrowinning of zinc
US4699696A (en) * 1986-04-15 1987-10-13 Omi International Corporation Zinc-nickel alloy electrolyte and process
US4717458A (en) * 1986-10-20 1988-01-05 Omi International Corporation Zinc and zinc alloy electrolyte and process
CN1023818C (en) * 1991-03-19 1994-02-16 昆明工学院 Vacuum distillation zinc extraction method of hot galvanizing residue
US5635051A (en) * 1995-08-30 1997-06-03 The Regents Of The University Of California Intense yet energy-efficient process for electrowinning of zinc in mobile particle beds
US6086691A (en) * 1997-08-04 2000-07-11 Lehockey; Edward M. Metallurgical process for manufacturing electrowinning lead alloy electrodes
CN1065919C (en) * 1998-04-24 2001-05-16 昆明理工大学 Vacuum distillation of hard zinc to extract zinc and to concentrate germanium, indium and silver

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4028199A (en) * 1974-08-05 1977-06-07 National Development Research Corporation Method of producing metal powder
US6238542B1 (en) * 1998-09-15 2001-05-29 Thomas Helden Water soluble brighteners for zinc and zinc alloy electrolytes
WO2000039367A2 (en) * 1998-12-23 2000-07-06 Half Tone Limited Solution and process for the electrodeposition of gold and gold alloys

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
MAGALHAES, A. C. ET AL: "Influence of Some Quaternary Ammonium Salts Upon Zinc Deposition on Steel From Acidic Methanesulfonate Electrolyte" BULLETIN OF ELECTROCHEMISTRY (2002), 18(5), 193-202 , vol. 18, no. 5, 1 May 2002 (2002-05-01), pages 193-202, XP009014801 *

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KR20040044443A (en) 2004-05-28
HK1075920A1 (en) 2005-12-30
WO2003016593A3 (en) 2003-10-09
CN1653209A (en) 2005-08-10
JP2004537653A (en) 2004-12-16
KR100599993B1 (en) 2006-07-13
RU2288299C2 (en) 2006-11-27
BR0211933A (en) 2004-10-26
CN100342061C (en) 2007-10-10
DE60203301T2 (en) 2006-04-13
DE60203301D1 (en) 2005-04-21
NO20040651L (en) 2004-04-16
RU2004107493A (en) 2005-06-10
ZA200405167B (en) 2005-06-27
MXPA04001459A (en) 2005-02-17
ES2238586T3 (en) 2005-09-01
EP1417357A2 (en) 2004-05-12
US20050011769A1 (en) 2005-01-20
AU2002322888B2 (en) 2007-06-21
EP1417357B1 (en) 2005-03-16
CA2457071C (en) 2007-05-29
CA2457071A1 (en) 2003-02-27

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