Process for the manufacture of sintered metal bodies, in particular battery electrodes

Claim 2

A process for the manufacture of sintered metal bodies comprising mixing a powdered metal or metal alloy with at least one pore-forming filler, said filler being a fine grain salt or mixture of salts, filling a mold with said mixture, heating the uncompressed mixture to the sintering temperature of the metal or metal alloy, reducing the pressure of the atmosphere surrounding said mold during said heating, the salt of said mixture being vaporizable under the conditions of sintering, said salt of the mixture being selected such that significant vaporization thereof occurs only after sintering of the metal has begun, continuing such heat and reduced pressure for a period of time sufficient to vaporize substantially all of said salt and sinter the metal or alloy into a porous body, and recovering the porous sintered metal.

Claim 3

A process for the manufacture of a positive sintered nickel electrode comprising the steps of providing a mixture of powdered nickel and a fine-grained salt vapourisable at the sintering temperature of the nickel, pouring said mixture into a sintering mould, embedding an electrode support in said mixture, sintering said uncompressed mixture with said electrode support therein under a vacuum, compacting the resultant body and providing in said body gas discharge grooves, and electrochemically depositing nickel hydroxide on the porous sintered nickel electrode used as cathode in an electrolytic bath containing nickel nitrate of the formula Ni(NO 3 ) 2 .6H 2 O and optionally cobalt nitrate of the formula Co(NO 3 ) 2 .6H 2 O in nitric acid solution, in which in that the deposition in the pores of the nickel cathode is carried out in a bath which contains from 120 g/l to 600 g/l of nickel nitrate and at the most 60 g/l of cobalt nitrate and which is maintained at a pH in the range of from 1 to 3 by the addition of nitric acid to provide a positive sintered nickel electrode.

Claim 4

A process for the manufacture of a positive sintered nickel electrode comprising the steps of providing a mixture of powdered nickel and a fine-grained salt vapourisable at the sintering temperature of the nickel, pouring said mixture into a sintering mould, embedding an electrode support in said mixture, sintering said uncompressed mixture with said electrode support therein under a vacuum, compacting the resultant body and providing in said body gas discharge grooves, and electrochemically depositing nickel hydroxide on the porous sintered nickel electrode used as cathode in an electrolytic bath containing nickel nitrate of the formula Ni(NO 3 ) 2 .6H 2 O and optionally cobalt nitrate of the formula Co(NO 3 ) 2 .6H 2 O in nitric acid solution, in which in that the deposition in the pores of the nickel cathode is carried out in a bath which contains from 120 g/l to 600 g/l of nickel nitrate and at the most 60 g/l of cobalt nitrate and which is maintained at a pH in the range of from 1 to 3 by the addition of nitric acid to provide a positive sintered nickel electrode.

Claim 5

A process as claimed in claim 1 in which the sintering is carried out at a temperature of between 300° C. and 1200° C.

Claim 6

A process as claimed in claim 1 in which a vacuum of at least 10 -2 bar is maintained during the sintering process.

Claim 7

A process as claimed in claim 1 in which a vacuum of from 10 -3 to 10 -6 bar is maintained during the sintering process.

Claim 8

A process as claimed in claim 1 in which a salt which is compatible with the metal is used as filler.

Claim 9

A process as claimed in claim 6 in which the salt is a halide.

Claim 10

A process as claimed in claim 7 in which the halide is a metal halide.

Claim 11

A process as claimed in claim 8 in which the halide is a sodium chloride.

Claim 12

A process as claimed in claim 1 in which the metals which are sintered are iron and nickel and mixtures thereof.

Claim 13

A process as claimed in claim 1 in which the metals which are sintered are copper, silver, manganese and/or cobalt.

Claim 14

A process as claimed in claim 1 in which the mixture of powdered metal and salt is used in a substantially dry form.

Claim 15

A process as claimed in claim 1 in which an electrode support is embedded in the mixture of powdered metal and salt and is sintered in with it.

Claim 16

A process as claimed in claim 1 in which the ratio by weight of metal to salt in the mixture is between 1:0.5 and 1:3, preferably between 1:1.15 and 1:5.

Claim 17

A process as claimed in claim 1 in which the metal powder is used in the form of particles measuring of up to 50 μm in size.

Claim 18

A process as claimed in claim 1 in which the particles of the metal powder have a size from 2 to 15 μm.

Claim 19

A process as claimed in claim 1 in which the powdered salt is used in a particle size of from 40 μm to 100 μm.

Claim 20

A process as claimed in claim 1 for the manufacture of a sintered iron electrode in which in that the particle size of the iron powder in the mixture is from 2 to 10 μm and the particle size of the salt powder is from 42 to 100 μm.

Claim 21

A process as claimed in claim 18 in which there is used an iron powder, one to which has been added approximately 1% by weight of iron sulphide powder (FeS).

Claim 22

A process as claimed in claim 1 for the manufacture of a sintered nickel electrode, in which the particle size of the nickel powder is 2 to 7 μm and the particle size of the salt powder is from 42 to 100 μm.

Claim 23

A process as claimed in claim 1 in which the vacuum is raised in the course of the sintering process.

Claim 24

A process as claimed in claim 1 in particular for the manufacture of sintered electrodes, including the step of compacting the sintered body obtained by the sintering process to between 95 and 50% of its original height before subsequent impregnation, and this compacting operation is preferably accompanied by the stamping in of parallel gas discharge grooves.

Claim 25

A process for the manufacture of a positive sintered nickel electrode by electrochemical deposition of nickel hydroxide on a porous sintered nickel electrode used as cathode in an electrolytic bath containing nickel nitrate of the formula Ni(NO 3 ) 2 .6H 2 O and optionally cobalt nitrate of the formula Co(NO 3 ) 2 .6H 2 O in nitric acid solution, in which in that the deposition in the pores of the nickel cathode is carried out in a bath which contains from 120 g/l to 600 g/l of nickel nitrate and at the most 60 g/l of cobalt nitrate and which is maintained at a pH in the range of from 1 to 3 by the addition of nitric acid.

Claim 26

A process for the manufacture of a positive sintered nickel electrode by electrochemical deposition of nickel hydroxide on a porous sintered nickel electrode used as cathode in an electrolytic bath containing nickel nitrate of the formula Ni(NO 3 ) 2 .6H 2 O and optionally cobalt nitrate of the formula Co(NO 3 ) 2 .6H 2 O in nitric acid solution, in which in that the deposition in the pores of the nickel cathode is carried out in a bath which contains from 120 g/l to 600 g/l of nickel nitrate and at the most 60 g/l of cobalt nitrate and which is maintained at a pH in the range of from 1 to 3 by the addition of nitric acid.

Claim 27

A process as claimed in claim 23 in which the electrolysis is carried out at temperatures of from 85° to 95° C.

Claim 28

A process as claimed in claim 24 in which a temperature of 90° to 95° C. is used.

Claim 29

A process as claimed in claim 23 in which the electrolysis is carried out at a current density of from 5 A/dm 2 to 15 A/dm 2 .

Claim 30

A process as claimed in claim 26 in which a current density of approximately 10 A/dm 2 is used.

Claim 31

A process as claimed in claim 23 in which the bath is kept in continuous motion and is regenerated and filtered outside its container.

Claim 32

A process as claimed in claim 23 in which the positive auxiliary electrodes used are graphite fleeces or plates.

Claim 33

A process as claimed in claim 23 in which in that the positive auxiliary electrodes used are nickel plates functioning as self consuming electrodes.

Claim 34

A process as claimed in claim 23 in which the positive auxiliary electrodes used are nickel plates produced from compacted nickel scrap.

Claim 35

A process as claimed in any of claims 23 to 31 in which in that the positive auxiliary electrodes are enveloped by pocket separators closed on three sides to prevent contamination of the bath electrolytes.

Claim 36

A process as claimed in any of claims 23 to 32 in which after electrolytic impregnation with nickel hydroxide, the sintered electrode is neutralised by immersion in 30% potassium hydroxide solution at 50° to 60° C. and then activated by immersion in 2 molar ammonium persulphate solution for approximately one hour at room temperature.