GB1104582A

GB1104582A – Improved method of electrolytically producing nickel powder
– Google Patents

GB1104582A – Improved method of electrolytically producing nickel powder
– Google Patents
Improved method of electrolytically producing nickel powder

Info

Publication number
GB1104582A

GB1104582A
GB52060/65A
GB5206065A
GB1104582A
GB 1104582 A
GB1104582 A
GB 1104582A
GB 52060/65 A
GB52060/65 A
GB 52060/65A
GB 5206065 A
GB5206065 A
GB 5206065A
GB 1104582 A
GB1104582 A
GB 1104582A
Authority
GB
United Kingdom
Prior art keywords
cathode
powder
anode
hours
ammonium hydroxide
Prior art date
1964-12-09
Legal status (The legal status 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 status listed.)

Expired

Application number
GB52060/65A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)

Allis Chalmers Corp

Original Assignee
Allis Chalmers Corp
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.)
1964-12-09
Filing date
1965-12-08
Publication date
1968-02-28

1965-12-08
Application filed by Allis Chalmers Corp
filed
Critical
Allis Chalmers Corp

1968-02-28
Publication of GB1104582A
publication
Critical
patent/GB1104582A/en

Status
Expired
legal-status
Critical
Current

Links

Espacenet

Global Dossier

Discuss

Classifications

C—CHEMISTRY; METALLURGY

C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR

C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR

C25C5/00—Electrolytic production, recovery or refining of metal powders or porous metal masses

C25C5/02—Electrolytic production, recovery or refining of metal powders or porous metal masses from solutions

Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS

Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE

Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE

Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather

Y02A50/30—Against vector-borne diseases, e.g. mosquito-borne, fly-borne, tick-borne or waterborne diseases whose impact is exacerbated by climate change

Abstract

In electrolytically producing finely divided Ni powder having a surface area in excess of 3m2/gm, electrolysis conditions include an aqueous electrolyte comprising 90 to 150 mls ammonium hydroxide per litre of solution, at least one Ni anode, at least one metallic cathode (e.g. of Ni or stainless steel which may be in mesh form), and a cathode current density of 0.007 to 0.090 amps/sq.cm. used for a period of 2 to 7 hours. After deposition the Ni powder is removed from the cathode. The ammonium hydroxide is the normal reagent grade having a concentration of 28 to 30 weight per cent of ammonia. After passing current for 2 to 3 hours, ammonium hydroxide may be added to the depleted solution, and current then be passed for a further 2 to 3 hours. The electrolyte may additionally contain NH4NO3, (NH4)2SO4 and/or nickel ammonium sulphate. The bath temperature may be from room temperature to 40 DEG C., and if the bath tends to become overheated the electrolysis may be periodically halted. The anode-cathode spacing may be 1/2 inch plus or minus 1/16 inch. After several successive depositions of Ni powder on a cathode, the cathode can be reconditioned by using it as an anode. The Ni powder can be used in fuel cell electrodes.

GB52060/65A
1964-12-09
1965-12-08
Improved method of electrolytically producing nickel powder

Expired

GB1104582A
(en)

Applications Claiming Priority (1)

Application Number
Priority Date
Filing Date
Title

US417214A

US3458407A
(en)

1964-12-09
1964-12-09
Method of producing nickel powder

Publications (1)

Publication Number
Publication Date

GB1104582A
true

GB1104582A
(en)

1968-02-28

Family
ID=23653053
Family Applications (1)

Application Number
Title
Priority Date
Filing Date

GB52060/65A
Expired

GB1104582A
(en)

1964-12-09
1965-12-08
Improved method of electrolytically producing nickel powder

Country Status (5)

Country
Link

US
(1)

US3458407A
(en)

DE
(1)

DE1483337A1
(en)

FR
(1)

FR1458849A
(en)

GB
(1)

GB1104582A
(en)

SE
(1)

SE324064B
(en)

Cited By (2)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

CN102912383A
(en)

*

2012-10-31
2013-02-06
南京工业大学
Method for manufacturing porous nickel powder by electro-deposition of Ni-Al-Mg-Li alloy

CN113122889A
(en)

*

2021-03-11
2021-07-16
上海应用技术大学
Preparation method of silver-polyaniline composite material for solar cell

Families Citing this family (4)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

US3510408A
(en)

*

1967-11-14
1970-05-05
Allis Chalmers Mfg Co
Process for producing high surface area nickel powder

US3852112A
(en)

*

1971-01-18
1974-12-03
Int Nickel Co
Activation of nickel battery plates

FR2402477A2
(en)

*

1977-09-09
1979-04-06
Anvar

NEW CATALYST FOR ELECTROLYTIC OXIDATION OF HYDROGEN

US4416745A
(en)

*

1982-03-01
1983-11-22
The Bendix Corporation
Process for recovering nickel from spent electroless nickel plating solutions

Family Cites Families (7)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

CA508160A
(en)

*

1954-12-14
R. Copson Harry
Electrodeposited nickel powder

US1442238A
(en)

*

1922-07-29
1923-01-16
Smith Albert Kelvin
Electrolytic apparatus

US2233103A
(en)

*

1938-04-06
1941-02-25
Hardy Metallurg Company
Production of nickel powder

US2625507A
(en)

*

1945-10-16
1953-01-13
Stuart A Mayper
Method of electrodepositing nickel

US3276921A
(en)

*

1962-09-24
1966-10-04
Michael W Freeman
Compositions and articles including non-pyrophoric microparticles

US3367801A
(en)

*

1964-01-10
1968-02-06
Texas Instruments Inc
Fuel cell including electrode of silver, nickel, and zinc

US3335033A
(en)

*

1964-08-27
1967-08-08
Gen Telephone & Elect
Method of making electric battery electrodes

1964

1964-12-09
US
US417214A
patent/US3458407A/en
not_active
Expired – Lifetime

1965

1965-12-08
DE
DE19651483337
patent/DE1483337A1/en
active
Pending

1965-12-08
SE
SE15878/65A
patent/SE324064B/xx
unknown

1965-12-08
GB
GB52060/65A
patent/GB1104582A/en
not_active
Expired

1965-12-08
FR
FR41439A
patent/FR1458849A/en
not_active
Expired

Cited By (3)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

CN102912383A
(en)

*

2012-10-31
2013-02-06
南京工业大学
Method for manufacturing porous nickel powder by electro-deposition of Ni-Al-Mg-Li alloy

CN102912383B
(en)

*

2012-10-31
2015-02-25
南京工业大学
Method for manufacturing porous nickel powder by electro-deposition of Ni-Al-Mg-Li alloy

CN113122889A
(en)

*

2021-03-11
2021-07-16
上海应用技术大学
Preparation method of silver-polyaniline composite material for solar cell

Also Published As

Publication number
Publication date

US3458407A
(en)

1969-07-29

SE324064B
(en)

1970-05-19

FR1458849A
(en)

1966-11-10

DE1483337A1
(en)

1969-03-13

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