GB1592063A - Creation of Inventions and Patents with Artificial Intelligence

GB1592063A – Sodium sulphur cells
– Google Patents

GB1592063A – Sodium sulphur cells
– Google Patents
Sodium sulphur cells

Download PDF
Info

Publication number
GB1592063A

GB1592063A
GB21709/77A
GB2170977A
GB1592063A
GB 1592063 A
GB1592063 A
GB 1592063A
GB 21709/77 A
GB21709/77 A
GB 21709/77A
GB 2170977 A
GB2170977 A
GB 2170977A
GB 1592063 A
GB1592063 A
GB 1592063A
Authority
GB
United Kingdom
Prior art keywords
substrate
carbon
current collector
nickel
cell
Prior art date
1978-05-08
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
GB21709/77A
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.)

Chloride Silent Power Ltd

Original Assignee
Chloride Silent Power Ltd
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.)
1978-05-08
Filing date
1978-05-08
Publication date
1981-07-01

1978-05-08
Application filed by Chloride Silent Power Ltd
filed
Critical
Chloride Silent Power Ltd

1978-05-08
Priority to GB21709/77A
priority
Critical
patent/GB1592063A/en

1978-05-22
Priority to US05/908,438
priority
patent/US4212933A/en

1978-05-22
Priority to DE19782822284
priority
patent/DE2822284A1/en

1978-05-22
Priority to JP6086278A
priority
patent/JPS54739A/en

1978-05-22
Priority to FR7815099A
priority
patent/FR2392508A1/en

1981-07-01
Publication of GB1592063A
publication
Critical
patent/GB1592063A/en

Status
Expired
legal-status
Critical
Current

Links

Espacenet

Global Dossier

Discuss

Classifications

H—ELECTRICITY

H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR

H05B—ELECTRIC HEATING; ELECTRIC LIGHT SOURCES NOT OTHERWISE PROVIDED FOR; CIRCUIT ARRANGEMENTS FOR ELECTRIC LIGHT SOURCES, IN GENERAL

H05B3/00—Ohmic-resistance heating

H05B3/10—Heater elements characterised by the composition or nature of the materials or by the arrangement of the conductor

H05B3/12—Heater elements characterised by the composition or nature of the materials or by the arrangement of the conductor characterised by the composition or nature of the conductive material

H05B3/14—Heater elements characterised by the composition or nature of the materials or by the arrangement of the conductor characterised by the composition or nature of the conductive material the material being non-metallic

H05B3/145—Carbon only, e.g. carbon black, graphite

H—ELECTRICITY

H01—ELECTRIC ELEMENTS

H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY

H01M4/00—Electrodes

H01M4/02—Electrodes composed of, or comprising, active material

H01M4/64—Carriers or collectors

H01M4/66—Selection of materials

H01M4/661—Metal or alloys, e.g. alloy coatings

H—ELECTRICITY

H01—ELECTRIC ELEMENTS

H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY

H01M4/00—Electrodes

H01M4/02—Electrodes composed of, or comprising, active material

H01M4/64—Carriers or collectors

H01M4/66—Selection of materials

H01M4/663—Selection of materials containing carbon or carbonaceous materials as conductive part, e.g. graphite, carbon fibres

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

Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION

Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation

Y02E60/10—Energy storage using batteries

Description

PATENT SPECIFICATION
Application No 21709/77 ( 22) Filed 23 May 1977 Complete Specification filed 8 May 1978
Complete Specification published 1 July 1981
INT CL 3 C 23 C 11/10 H Oi M 10/39 Index at acceptance C 7 F 1 A IB 5 2 Z 5 3 E 4 D 4 E 4 F HIB 1039 ( 11) ( 19) 1592063 ( 72) Inventors TREVOR LESLIE MARKIN, ROGER JOHN BONES, KEITH RADFORD LINGER, PETER JOHN BINDIN, MICHAEL PATRICK JOSEPH BRENNAN and GEOFFREY JOHN MAY ( 54) IMPROVEMENTS IN OR RELATING TO SODIUM SULPHUR CELLS ( 71) We, CHLORIDE SILENT POWER LIMITED, a British Company of 52 Grosvenor Gardens, London SWIW OAU, do hereby declare the invention, for which we pray that a patent may be granted to us, and the method by which it is to be performed, to be particularly described in and by the following statement:-
This invention relates to sodium sulphur cells and is concerned more particularly with the cathode current collector in such a cell.
In a sodium sulphur cell a solid electrolyte, for example a beta-alumina ceramic, separates an anodic region containing sodium which is liquid at the operating temperature of the cell from a cathodic region which, at the operating temperature, contains liquid sulphur and sodium polysulphides During discharge of the cell sodium ions pass through the electrolyte forming sodium polysulphides The cathodic reatant comprising the sulphur and polysulphides has a high electrical resistance and it is the practice to put a matrix packing of conductive material, for example carbon or graphite felt, in the cathodic region to provide electronic conduction Such graphite felt in itself has a relatively high resistance and it is desirable to keep the electronic current path through this material to the minimum length For that reason, this matrix material is arranged to extend between the surface of the electrolyte material and an adjacent surface of a current collector In a cell design where the sulphur is contained inside a tube of electrolyte material, this current collector may be a rod or composite rod disposed axially inside the electrolyte tube The current collector rod has to provide a high conductivity path between the matrix packing material and an external terminal of the cell It must however be chemically and electrochemically inert to the cathodic reactant material Metals such as aluminium and copper are sufficiently conductive but aluminium is passivated and copper is corroded after a few charge and discharge cycles of the cell Stainless steel, which is much less conductive than aluminium or copper, is also corroded after a few charge/discharge cycles For various reasons such corrosion causes a deterioration of cell characteristic The mechanism of the deterioration is not completely understood and is probably different for each material Certain nickel based alloys, in particular Inconel (Registered Trade Mark) (a nickel alloy containing some 13 % Cr 6 % Fe by weight together with minor constituents) have longer lives.
For this reason, carbon, particularly in its graphitic form, has been used as a current collector in many laboratory cells Carbon in itself however is not sufficiently conductive to be used alone in long cells which are operated at useful rates of charge and discharge Other materials which are thermodynamically stable in sulphur and polysulphides to the anode and cathode conditions that prevail in a sodium sulphur cell have been proposed A ceramic formed of oxides such as tantalum or niobium doped rutile is an example of such a thermodynamically stable material which can be used Nickel oxide doped with lithium oxide and lanthanium strontium cobaltite may be used Conductive ceramics are described in British Patent Specification No 1471914 However such materials are not sufficiently conductive to be used alone in large cells which operate at useful rates of charge and discharge.
It has therefore been proposed to use composite current collectors United States Patent Specification No 3982959 describes the use, in a sodium sulphur cell, of a cathode current collector of rod-like form arranged axially inside a solid electrolyte tube which contains the cathodic reactant and packing material, this current collector comprising a carbon tube with a metal core.
It is necessary to provide a deformable ( 21) ( 23) ( 44) ( 51) ( 52) 1,592,063 electronically-conductive interface in the annular region between the carbon tube and the metal core in order to ensure good electrical contact across this region despite temperature cycling of the cell Composites of this nature do raise manufacturing problems and it is difficult to construct such composites to have a useful life in a sodium sulphur cell It would be preferable to have the corrosion-resistant material as a protective layer on a conductive substrate which has other useful characteristics such as being readily formed by drawing or rolling, readily weldable or having an expansion coefficient well matched to that of the ceramic electrolyte Molybdenum is a corrosion-resistant material which is conductive but it is deficient in some of these useful properties mentioned above It is sometimes convenient to use a protective coating of molybdenum on a substrate It appears that molybdenum is corrosion-resistant in the cathodic reactant of a sodium sulphur cell because of the formation of a stable surface film of molybdenum disulphide which is also electronically conductive.

Claims (22)

Claims have been made for the efficacy of
simple coatings of carbon carried out by the application of collodial suspensions and of molybdenum coatings by the method of plasma spraying on substrates of steel, aluminium or iron-nickel-cobalt alloys but those skilled in the art know that such coatings have only transitory efficacy in the cathode electrodes of the devices previously described Plasma-sprayed molybdenum can be made to adhere to aluminium but the deposit is porous and the corroding species are able to penetrate through the porous layer to attack the substrate In the case of a current collector formed by plasma spraying an aluminium rod with molybdenum, the resistance of a sodium sulphur cell containing such a current collector in the cathode increases enormously over about 20 charge/discharge cycles and is not therefore suitable for commercial cells.
It has also been suggested that a stable cell resistance can be achieved if a conductive substrate of aluminium is protected by a polyphenylene resin which is impregnated with carbon to confer the marginal conducting properties which are required in the corrosion-resistant sheath of the composite current collecting member It is known however that the beneficial results of such a composite are much too transitory to find use in a practical energy conversion device.
The present invention makes use, in forming a current collector, of a coating technique known as plasma activated vapour deposition (PAVD) in which a plasma is used as a medium for chemical reaction and deposition of an electronically-conductive coating on an electronically-conductive substrate.
This technique makes use of the decomposition of a gas in an electrically-induced plasma, the substrate being connected as an electrode in a vessel containing an ionizable gas at a pressure such that a glow discharge 70 can be generated in the vessel, the conditions of operation being controlled to tend to cause the positive region to be confined adjacent to the substrate thereby causing deposition on the substrate of an element or elements in 75 combination from the ionizable gas By this technique it has been found possible to obtain highly adherent and stable coatings of electrically-conductive materials onto a conductive substrate Related techniques are 80 disclosed in the paper “Codeposition of Glassy Silica and Germania inside a Tube by Plasma-Activated CVD” by D Kuppers et al Journal of the Electrochemical Society Vol 123 No 7 pages 1079-82 July 1976 85 Thus, considered broadly, according to this invention, there is provided a cathode current collector for a sodium-sulphur cell comprising a substrate of electrically-conductive material coated with carbon pro 90 duced by decomposition of a carbon-containing gas in a glow discharge with the substrate heated to a temperature of ‘C-1000 C in an electric field.
The substrate may conveniently be of 95 nickel or a nickel-containing metal alloy, e g.
a nickel-chromium-iron alloy such as Inconel 600 (Registered Trade Mark) Inconel 600 is an alloy comprising, by weight, 72 % nickel, 14-17 % chromium, 6-10 % iron, not 100 more than 0 15 % carbon, not more than 1 % manganese, not more than 0 015 % sulphur, not more than 0 5 % silicon and not more than 0 5 % copper With some materials, e g.
aluminium, it is desirable to coat the sub 105 strate, e g with molybdenum, before applying the carbon.
The above-described current collector having a carbon coating deposited by a plasma activated vapour deposition (PAVD) 110 process has been found to have unexpected mechanical integrity and durability even when the coating is applied to a substrate which has a coefficient of thermal expansion differing widely from the coefficient of ther 115 mal expansion of the carbon coating material.
In considering current collectors and other components of an electrochemical cell having a PAVD deposited coating, it is conve 120 nient to consider individually the substrate material, the outer corrosion-resistant coating and, if provided, one or more intermediate layers separately The substrate in the case of a current collector would have to 125 have the required electronic conductivity.
For other components in the cell, the expansion coefficient may be important or the ease of fabrication This substrate material can be chosen without consideration of corrosion 130 1,592,063 resistance and typical substrates might be aluminium, copper, steel and iron nickel cobalt alloys As is well-known, by proper choice of the material of iron-nickel-cobalt S alloys, it is possible to obtain controlled expansion coefficients and it is thus possible, by choice of the substrate material, to match the expansion coefficient to that of some other component such as for example ceramic electrolyte material The outer layer is carbon which is chosen primarily by consideration of corrosion-resistance.
As indicated above one or more intermediate layers may be required in certain cases.
Such layers may be formed for example of nickel alloys such as Inconel 600 or nickel chromium alloys or chromium or molybdenum or chromium carbide or titanium carbide or silicon carbide The choice of the intermediate layer will primarily be governed by the materials chosen for the substrate and the outer layer, the intermediate layer being a material which can be deposited on the substrate, or on an already deposited layer and which will receive the outer layer or a further intermediate layer.
As mentioned above, carbon is of primary interest for the outer corrosion-resistant layer in a sodium sulphur cell It may be applied to a metal substrate and it has been found preferable to apply the carbon as a thin layer onto a smooth substrate of a metal having a coefficient of thermal expansion close to that of the carbon Suitable materials in this respect are Nilo-K (Registered Trade Mark), molybdenum, titanium and tungsten Nilo-K is a ternary nickel-cobalt-iron alloy containing 29 5 % nickel and 17 0 % cobalt by weight.
The substrate may be formed of one of these materials or such a material may be an intermediate layer formed as a coating on a substrate of a relatively inexpensive material such as mild steel Metals such as molybdenum and tungstem have a particular advantage as a substrate or as an intermediate layer under a carbon coating in that they are passive to the cathodic reactant of a sodium sulphur cell in the event of a local breakdown of the carbon layer The carbon is applied by a PAVD process as described above The intermediate layer may be applied by a PAVD process or by an ion beam technique Good coatings are also obtained on Inconel 600 although it has a relatively high coefficient of expansion.
The invention furthermore includes within its scope a method of making a cathode current collector for a sodium-sulphur cell comprising the steps of subjecting an electrically-conductive substrate to an electrical discharge in an atmosphere including a carbon-containing gas, the substrate being heated to a temperature of 200 ‘C-1000 C and the atmosphere being such that carbon deposition occurs on the substrate because of decomposition of the carbon-containing gas.
This carbon-containing gas is conveniently ethylene or carbon disulphide An inert carrier gas, e g argon or krypton is preferably provided to promote formation of the 70 glow discharge and to provide ions for ion bombardment of the article This ion bombardment consists in the forming of an adherent coating.
The pressure of said atmosphere may be 75 between 100 millitorr and 10 torr and, more preferably, is between 0 1 torr and 10 torr.
The following is a description of one method of forming a cathode current collector rod for a sodium-sulphur cell, reference 80 being made to the accompanying drawing which is a diagram illustrating the manufacture of the cathode current collector.
Referring to the drawing, the collector 10, e.g of molybdenum, is of generally rod like 85 form with an enlarged diameter part 9 near one end This collector is suspended coaxially in a cylindrical silica or glass reaction vessel 11, typically having a diameter of 40 to mm, which is arranged with its axis 90 upright The vessel 11 is surrounded by a helical water-cooled copper coil 12 which is coupled to a high frequency generator 13.
The spacing between adjacent turns of the coil 12 is typically 15 mm, and the diameter 95 of the coil is about 100 mm The collector 10 is suspended so that only the narrow diameter portion lies within the coil as, in this particular construction, only this narrow diameter part is to be coated with carbon 100 The vessel 11 has controlled inlets 14, 15 for reactant gases and an outlet 16 leading to a pump.
The reactor vessel 11 is evacuated to about 0.02 torr and then filled with an inert gas e g 105 argon to 2 0 torr and the pressure maintained at that level by adjustment of a throttle valve 17 in the pumping line The high frequency power is then applied to the coil 12 typically at 1 2 k V and a plasma sheath develops 110 around the collector 10 which is coupled to earth (or may be biased negatively) After 15 to 30 minutes, when the collector 10 has reached thermal equilibrium and the surface thereof has been cleaned by bombardment 115 with inert gas ions, the carbon containing reactant gas, e g ethylene, is let into the vessel 11, the pressure being adjusted and controlled to maintain a pressure of 2 0 to 2 5 torr Carbon is now deposited on the collec 120 tor; the coating time determines the thickness, the rate of deposition being constant.
Typically 45 minutes would give I to 2 gm coating.
The reactant gas and the power are turned 125 off, then the argon, and the system evacuated The collector 10 then cools under vacuum The temperature which it has reached is determined by the currents induced in the skin of the material by the high 130 1,592,063 frequency Factors affecting this temperature include the power to the coil, the dimensions of the coil and the collector, the material of the collector and the frequency applied.
The reactant gas for this example is ethylene, which is fed in at 30 ml min-‘, together with argon as the carrier inert gas which is fed in at 95 ml min-1.
It has been found that with this technique, the collector is uniformly coated with a very fine carbon which is essentially amorphous, having an extremely fine crystallite size, of low modulus and strongly adherent to the collector.
The following are two examples of test results obtained with sodium sulphur cells employing current collectors formed as described above.
EXAMPLE 1 A molybdenum rod current collector was coated with carbon by the plasma activated vapour deposition method described above.
The current collector was employed in a cell in which the sulphur was contained inside a tubular solid ceramic electrolyte of betaalumina with the sodium outside the electrolyte tube This cell completed 135 cycles during 35 days at 100 m A cm-2 discharge current intensity and 50 m A cm-2 charge current density before electrolyte failure occurred There was no rise in cell resistance during the 135 cycles and in this respect the cell shows a distinct advantage over similar cells run to date The capacity remained at 76 % of the theoretical based on the weight of sulphur in the electrode Cells containing a molybdenum rod current collector without a carbon coating show a rapid loss of capacity with cycling.
EXAMPLE 2 As molybdenum is expensive, a current collector was made having a mild steel substrate with a thin film ( 25 glm) of molybdenum applied over its surface by a soft vacuum deposition method The molybdenum layer was protected by a coating of carbon put down by the PAVD method described above The cell embodying this current collector completed 220 cycles during 52 days (and continued to run) at 100 m A cm-2 discharge and 50 m A cm-2 charge current density The capacity remains constant at 73 % of theoretical based on the weight of sulphur in the electrode The resistance of the cell has remained constant.
The behaviour of the cell is therefore much akin to the cell in Example 1 Apart from the use of the cheaper substrate, the current collector is constructed in the same way It has been found that PAVD carbon layers deposited onto smooth layers, such as result from vapour deposition methods, are better than coatings on a rougher surface such as a surface resulting from plasma spraying.
If the current collector is long, it may be desirable to provide the mild steel with a core of a good electrically conducting material such as aluminium or copper.
It is convenient to use a radio frequency field so that the substrate is inductively heated If alternative heating means are provided, there is no need to have a coil and thus the radio frequency power may be applied to two electrodes or between one electrode and the article to be coated Instead of a radio frequency field, in this case a D C.
field may be employed With a D C field, conveniently the article forms one electrode and the second electrode is in the form of a cylinder, conveniently of mesh material, inside the evacuated vessel In some cases, the article may be arranged in the field between two electrodes Using electrodes instead of a coil, it becomes readily possible to obtain more intense fields and the substrate may be heated by the electrical discharge.
WHAT WE CLAIM IS:1 A cathode current collector for a sodium-sulphur cell comprising an electrically conductive substrate coated with carbon produced by decomposition of a carbon 95 containing gas in a glow discharge with the substrate heated to a temperature of ‘C-1000 ‘C in an electric field.

2 A cathode current collector as claimed in claim 1 wherein the substrate is nickel or a 100 nickel-containing metal alloy.

3 A cathode current collector as claimed in claim 1 wherein the substrate is of a nickel-chromium-iron alloy.

4 A cathode current collector as claimed 105 in claim 3 wherein the substrate is an alloy containing, by weight, 72 % nickel, 14-17 % chromium, 6-10 % iron, not more than 0.15 % carbon, not more than 1 % manganese, not more than 0 015 % sulphur, not more than 110 0.

5 % silicon and not more than 0 5 % copper.
A method of making a cathode current collector for a sodium-sulphur cell comprising the steps of subjecting an electrically conductive substrate to an electrical dis 115 charge in an atmosphere including a carboncontaining gas, the substrate being heated to a temperature of 200 ‘C-1000 C and the atmosphere being such that carbon deposition occurs on the substrate because of 120 decomposition of the carbon-containing gas.

6 A method as claimed in claim 5 wherein the temperature of the substrate is between 400 C and 1000 C.

7 A method as claimed in claim 5 125 wherein the temperature of the substrate is between 400 ‘C and 600 ‘C.

8 A method as claimed in any of claims to 7 wherein the electric discharge is produced by a radio frequency field 130 1,592,063

9 A method as claimed in claim 8 wherein the substrate is inductively heated by the radio frequency field.

A method as claimed in any of claims 5 to 7 wherein the electric discharge is produced by a direct voltage between an electrode around the substrate and the substrate or between two electrodes.

11 A method as claimed in any of claims 5 to 10 wherein said atmosphere includes an inert gas to promote the formation of a glow discharge.

12 A method as claimed in claim 11 wherein the inert gas is argon.

13 A method as claimed in any of claims to 12 wherein the carbon-containing gas is ethylene or carbon disulphide.

14 A method as claimed in either claim 12 or claim 13 wherein the carbon-containing gas is introduced after the arc has been struck in the argon.

A method as claimed in any of claims to 14 wherein the pressure of said atmosphere is between 10 millitorr and 10 torr.

16 A method as claimed in claim 15 wherein the pressure is between 0 1 torr and torr.

17 A method as claimed in any of claims to 16 wherein the substrate is a nickel or a nickel-containing alloy.

18 A method as claimed in any of claims to 16 wherein the substrate is a nickelchromium-iron alloy.

19 A method as claimed in any of claims 5 to 16 wherein the substrate is an alloy comprising by weight, 72 % nickel, 14-17 % chromium, 6-10 % iron, not more than 0.15 % carbon, not more than 1 % manganese, not more than 0 015 % sulphur, not more than 0 5 % silicon and not more than 0 5 % copper.

A method as claimed in any of claims to 16 wherein the substrate is a molybdenum-coated metal.

21 A method of making a cathode current collector for a sodium sulphur cell substantially as hereinbefore described with reference to the accompanying drawing.

22 A cathode current collector for a sodium sulphur cell made by the method of any of claims 5 to 21.
BOULT, WADE & TENNANT, Chartered Patent Agents, 34 Cursitor Street, London EC 4 A 1 PQ.
Printed for Her Majesty’s Stationery Office by Burgess & Son (Abingdon) Ltd 1981 Published at The Patent Office, Southampton Buildings, London WC 2 A LAY.
from which copies may be obtained.

GB21709/77A
1977-03-23
1978-05-08
Sodium sulphur cells

Expired

GB1592063A
(en)

Priority Applications (5)

Application Number
Priority Date
Filing Date
Title

GB21709/77A

GB1592063A
(en)

1978-05-08
1978-05-08
Sodium sulphur cells

US05/908,438

US4212933A
(en)

1977-03-23
1978-05-22
Current collector for electrochemical cells and method of making

DE19782822284

DE2822284A1
(en)

1978-05-08
1978-05-22

CATHODE COLLECTOR FOR A SODIUM SULFUR CELL

JP6086278A

JPS54739A
(en)

1978-05-08
1978-05-22
Positiveeelectrode collector of sodiumm sulfur battery and method of manufacture thereof

FR7815099A

FR2392508A1
(en)

1978-05-08
1978-05-22

SODIUM SULFUR BATTERY IMPROVEMENTS

Applications Claiming Priority (1)

Application Number
Priority Date
Filing Date
Title

GB21709/77A

GB1592063A
(en)

1978-05-08
1978-05-08
Sodium sulphur cells

Publications (1)

Publication Number
Publication Date

GB1592063A
true

GB1592063A
(en)

1981-07-01

Family
ID=10167522
Family Applications (1)

Application Number
Title
Priority Date
Filing Date

GB21709/77A
Expired

GB1592063A
(en)

1977-03-23
1978-05-08
Sodium sulphur cells

Country Status (5)

Country
Link

US
(1)

US4212933A
(en)

JP
(1)

JPS54739A
(en)

DE
(1)

DE2822284A1
(en)

FR
(1)

FR2392508A1
(en)

GB
(1)

GB1592063A
(en)

Cited By (4)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

GB2122224A
(en)

1982-06-23
1984-01-11
Atomic Energy Authority Uk
Ion beam carbon layers

GB2155496A
(en)

1984-03-03
1985-09-25
Standard Telephones Cables Ltd
Pulsed plasma coating process

GB2164581A
(en)

1982-04-13
1986-03-26
Michael Paul Neary
Chemical method

GB2200138A
(en)

1984-07-26
1988-07-27
Japan Res Dev Corp
Semiconductor crystal growth apparatus

Families Citing this family (16)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

SE8004352L
(en)

1979-06-14
1980-12-15
Atomic Energy Authority Uk

TRANSMISSION ELEMENT AND SYSTEM

DE3117381A1
(en)

1981-05-02
1982-11-18
Brown, Boveri & Cie Ag, 6800 Mannheim

“ELECTROCHEMICAL STORAGE CELL OR RELATIVE BATTERY”

JPS57202449A
(en)

1981-06-04
1982-12-11
Toshiba Corp
Manufacture of heat collecting body

DE3225873A1
(en)

1982-07-10
1984-01-12
Brown, Boveri & Cie Ag, 6800 Mannheim
Method of producing an electrochemical storage cell

DE3615240A1
(en)

1986-05-06
1987-11-12
Bbc Brown Boveri & Cie

ELECTROCHEMICAL STORAGE CELL

US4756964A
(en)

1986-09-29
1988-07-12
The Dow Chemical Company
Barrier films having an amorphous carbon coating and methods of making

DE3744170A1
(en)

1987-12-24
1989-07-06
Asea Brown Boveri

ELECTROCHEMICAL STORAGE CELL

GB9007998D0
(en)

1990-04-09
1990-06-06
Aabh Patent Holdings
Electrochemical cell

US4999262A
(en)

1990-04-20
1991-03-12
Hughes Aircraft Company
Multilayer cathode current collector/container for a battery

GB2250629A
(en)

1990-11-23
1992-06-10
Chloride Silent Power Ltd
Battery of high temperature cells

CA2077773A1
(en)

1991-10-25
1993-04-26
Thomas R. Anthony
Microwave, rf, or ac/dc discharge assisted flame deposition of cvd diamond

US5643639A
(en)

1994-12-22
1997-07-01
Research Triangle Institute
Plasma treatment method for treatment of a large-area work surface apparatus and methods

US5609912A
(en)

1995-09-08
1997-03-11
Georgia Tech Research Corp.
Ceramic fabric forming method

CA2412107A1
(en)

2001-11-14
2003-05-14
Wilson Greatbatch Technologies, Inc.
Carbon-coated titanium current collectors for use in alkali metal electrochemical cells

CN103165900B
(en)

2011-12-08
2016-03-30
通用电气公司
A kind of alkali metal-metal halide battery

CN112551044B
(en)

2020-12-10
2022-09-27
惠州市恒泰科技股份有限公司
Method and device for feeding to-be-formed battery cell

Family Cites Families (7)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

US3177094A
(en)

1961-07-14
1965-04-06
Philips Corp
Method for coating a molybdenum wire with a carbon layer and the coated article

US3658572A
(en)

1968-11-05
1972-04-25
Westinghouse Electric Corp
Pyrolytic coatings of molybdenum sulfide by plasma jet technique

US4142008A
(en)

1972-03-01
1979-02-27
Avco Corporation
Carbon filament coated with boron and method of making same

NO750445L
(en)

1974-02-15
1975-08-18
Electricity Council

GB1444519A
(en)

1974-08-03
1976-08-04
English Electric Valve Co Ltd
Grid electrodes

IT1070563B
(en)

1975-11-14
1985-03-29
Ibm

IMPROVED EQUIPMENT FOR ION IMPLANTATION

US3985575A
(en)

1976-01-30
1976-10-12
Ford Motor Company
Secondary battery or cell with dual electrode

1978

1978-05-08
GB
GB21709/77A
patent/GB1592063A/en
not_active
Expired

1978-05-22
JP
JP6086278A
patent/JPS54739A/en
active
Pending

1978-05-22
DE
DE19782822284
patent/DE2822284A1/en
not_active
Withdrawn

1978-05-22
US
US05/908,438
patent/US4212933A/en
not_active
Expired – Lifetime

1978-05-22
FR
FR7815099A
patent/FR2392508A1/en
not_active
Withdrawn

Cited By (5)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

GB2164581A
(en)

1982-04-13
1986-03-26
Michael Paul Neary
Chemical method

GB2122224A
(en)

1982-06-23
1984-01-11
Atomic Energy Authority Uk
Ion beam carbon layers

GB2155496A
(en)

1984-03-03
1985-09-25
Standard Telephones Cables Ltd
Pulsed plasma coating process

GB2200138A
(en)

1984-07-26
1988-07-27
Japan Res Dev Corp
Semiconductor crystal growth apparatus

GB2200138B
(en)

1984-07-26
1989-05-10
Japan Res Dev Corp
Semiconductor crystal growth apparatus

Also Published As

Publication number
Publication date

JPS54739A
(en)

1979-01-06

DE2822284A1
(en)

1978-12-07

US4212933A
(en)

1980-07-15

FR2392508A1
(en)

1978-12-22

Contact information