High rate sealed lead-acid battery with ultrathin plates

Claim 2

A normally sealed rechargeable lead-acid cell of the starved electrolyte type which internally recombines oxygen on charging, comprising: porous positive and negative electrode plates, each having major faces and a thickness of from about 0.007 to about 0.027 inches and formed of electrochemically active material respectively joined to high hydrogen overvoltage foraminous lead grids, each grid having a thickness of from about 0.005 inches to no more than 0.019 inches; porous, electrolyte-absorbent compressible separator interposed between the positive and negative plates and compressed against the major faces of such plates to define, in combination, a cell pack; the geometric surface area of the major faces of such plates being at least about 28 square inches per cubic inch of volume of the cell pack; liquid acid electrolyte in a starved amount absorbed in the pores of the plates and separator; and a container encapsulating the cell pack in a normally sealed configuration.

Claim 3

The lead-acid cell of claim 1 wherein the average spacing between the positive and negative electrode plates in the cell pack is from about 0.005 to 0.020 inches.

Claim 4

The lead-acid cell of claim 1 wherein the ratio of the average spacing between the plates to the thickness of the negative plate is less than about 0.8.

Claim 5

The lead-acid cell of claim 1 wherein the grid of the negative plate has a minimum Pb purity of at least 99.9 percent by weight.

Claim 6

A normally sealed rechargeable lead-acid cell of the recombinant type, comprising: porous positive and negative electrode plates having substantially equal thicknesses in the range from about 0.007 to about 0.027 inches and formed of electrochemically active material respectively pasted on high hydrogen overvoltage foraminous lead grids, each grid having a thickness of from about 0.005 inches to no more than 0.019 inches; porous, electrolyte-absorbent compressible separator interposed between the positive and negative plates and compressed there against under firm mutual stacking pressure; the average spacing between opposite polarity plates being between about 0.005 and about 0.020 inches; liquid electrolyte in a starved amount absorbed in the pores of the plates and separator; and a container encapsulating the plates and separators in a normally sealed configuration.

Claim 7

A normally sealed rechargeable lead-acid cell of the recombinant type, comprising: porous positive and negative electrode plates having substantially equal thicknesses in the range from about 0.007 to about 0.027 inches and formed of electrochemically active material respectively pasted on high hydrogen overvoltage foraminous lead grids, each grid having a thickness of from about 0.005 inches to no more than 0.019 inches; porous, electrolyte-absorbent compressible separator interposed between the positive and negative plates and compressed there against under firm mutual stacking pressure; the average spacing between opposite polarity plates being between about 0.005 and about 0.020 inches; liquid electrolyte in a starved amount absorbed in the pores of the plates and separator; and a container encapsulating the plates and separators in a normally sealed configuration.

Claim 8

The lead-acid cell of claim 5 wherein the ratio of the average spacing between the plates to the thickness of the negative plate is less than about 0.8.

Claim 9

The lead acid cell of claim 5 wherein the grid of the negative plate has a minimum Pb purity of at least 99.9 percent by weight.

Claim 10

The lead-acid cell of claim 5 wherein the separator is comprised of a mat of acid-wettable binderfree glass fibers, individual fibers of which have average diameters of from about 0.2 to about 10 microns, and the mat having a porosity of from about 85 to about 95 percent.

Claim 11

The lead-acid cell of claim 5 wherein a thin layer of electrolyte is homogeneously distributed throughout the negative plate.

Claim 12

A normally sealed rechargeable lead-acid cell of the starved electrolyte type which internally recombines oxygen on charging, comprising: porous positive and negative electrode plates, each having major faces and thickness of from about 0.007 to about 0.027 inches and formed of electrochemically active material respectively pasted on high hydrogen overvoltage foraminous lead grids having a purity of at least about 99.9 percent by weight lead, each grid having a thickness of from about 0.005 inches to no more than 0.019 inches; porous, electrolyte-absorbent compressible separator of silica base and having a surface area (BET method) of from about 0.1 to about 20 m 2 /g, interposed between the positive and negative plates and compressed against the major faces of such plates to define, in combination, a cell pack; the geometric surface area of the major faces of such plates being at least about 28 square inches per cubic inch of volume of the cell pack; liquid acid electrolyte in a starved amount absorbed in the pores of the plates and separator; and a container encapsulating the cell pack in a normally sealed configuration.

Claim 13

A normally sealed rechargeable lead-acid cell of the starved electrolyte type which internally recombines oxygen on charging, comprising: porous positive and negative electrode plates, each having major faces and thickness of from about 0.007 to about 0.027 inches and formed of electrochemically active material respectively pasted on high hydrogen overvoltage foraminous lead grids having a purity of at least about 99.9 percent by weight lead, each grid having a thickness of from about 0.005 inches to no more than 0.019 inches; porous, electrolyte-absorbent compressible separator of silica base and having a surface area (BET method) of from about 0.1 to about 20 m 2 /g, interposed between the positive and negative plates and compressed against the major faces of such plates to define, in combination, a cell pack; the geometric surface area of the major faces of such plates being at least about 28 square inches per cubic inch of volume of the cell pack; liquid acid electrolyte in a starved amount absorbed in the pores of the plates and separator; and a container encapsulating the cell pack in a normally sealed configuration.

Claim 14

The lead-acid cell of claim 10 wherein liquid sulfuric acid electrolyte is employed having a specific gravity of from about 1.300 to 1.380, in the charged condition of the cell.

Claim 15

The lead-acid cell of claim 10 wherein the geometric surface area of the major faces of such plates are at least about 35 square inches per cubic inch of volume of the cell pack.

Claim 16

The lead-acid cell of claim 10 wherein the average spacing between the positive and negative electrode plates in the cell pack is from about 0.005 to 0.020 inches.

Claim 17

The lead-acid cell of claim 1 wherein the average spacing between the positive and negative electrode plates in the cell pack is from about 0.010 to about 0.018 inches.

Claim 18

The lead-acid cell of claim 1 wherein the ratio of the average spacing between the plates to the thickness of the negative plate is from about 0.5 to about 1.0.

Claim 19

The lead-acid cell of claim 1 employing liquid sulfuric acid electrolyte having a specific gravity of from about 1.300 to about 1.380, in the charged condition of the cell.

Claim 20

The lead-acid cell of claim 1 wherein each grid has a thickness of from about 0.009 to about 0.017 inches.

Claim 21

The lead-acid cell of claim 5 wherein each grid has a thickness of from about 0.009 to about 0.017 inches.

Claim 22

The lead-acid cell of claim 10 wherein each grid has a thickness of from about 0.009 to about 0.017 inches.

Claim 23

The lead-acid cell of claim 1 wherein the cell has a minimum cycle life on the order of 200 cycles (one cycle per day regime, recharge at constant voltage and then discharge at C/5 rate to 1.60V cutoff), with the positive grid still being intact after such 200 cycles.

Claim 24

The lead-acid cell of claim 5 wherein the cell has a minimum cycle life on the order of 200 cycles (one cycle per day regime, recharge at constant voltage and then discharge at C/5 rate to 1.60V cutoff), with the positive grid still being intact after such 200 cycles.

Claim 25

The lead-acid cell of claim 10 wherein the cell has a minimum cycle life on the order of 200 cycles (one cycle per day regime, recharge at constant voltage and then discharge at C/5 rate to 1.60V cutoff), with the positive grid still being intact after such 200 cycles.

Claim 26

The lead-acid cell of claim 20 wherein there is substantially no evidence of corrosion of such positive grid after 200 cycles.

Claim 27

The lead-acid cell of claim 21 wherein there is substantially no evidence of corrosion of such positive grid after 200 cycles.

Claim 28

The lead-acid cell of claim 22 wherein there is substantially no evidence of corrosion of such positive grid after 200 cycles.