BN Bonded BN fiber article from boric oxide fiber

Claim 3

The method claimed in claim 1 wherein from about 2 to about 20 weight percent of boric acid is blended with from about 80 to about 98 weight percent of fiber.

Claim 4

The method of claim 2 wherein the boric acid is in particulate form.

Claim 5

The method claimed in claim 1 wherein the heating to melt the boric acid and the heating to convert boric acid and boron oxide to boron nitride are done simultaneously in an ammonia atmosphere.

Claim 6

The method of claim 2 wherein the boric acid is orthoboric acid.

Claim 7

The method of claim 2 wherein the boric acid is tetraboric acid.

Claim 8

The method of claim 6 wherein said article is heated to between about 160° C. and about 460° C. for from about three minutes to about three hours to melt the boric acid and said gas is an inert gas or nitrogen.

Claim 9

The method of claim 7 wherein the sufficient temperature to convert boric acid and boron oxide is from about 200° C. to about 900° C. and the sufficient conversion time is from about 2 to about 24 hours.

Claim 10

The method of claim 8 wherein said boric acid is in particulate form and the average particle size is below about 100μ.

Claim 11

The method claimed in claim 2 wherein from about 80 to about 90 weight percent boron oxide fiber is blended with from about 10 to about 20 weight percent of boric acid and said heating temperature is from about 240° C. to about 265° C.

Claim 12

The method claimed in claim 2 wherein the fibers are blended with boric acid by slurrying the fibers and boron oxide in an anhydrous liquid and removing the liquid from the fibers.

Claim 13

The method claimed in claim 11 wherein the liquid is petroleum distillate having a boiling point below about 100° C. and the liquid is removed by evaporation.

Claim 14

The method claimed in claim 2 wherein the fibers and boric acid are blended by blowing them randomly into a container.

Claim 15

The method claimed in claim 2 wherein the fibers and boric acid are blended by mixing them in a fluidized bed.

Claim 16

The method of claim 1 wherein the shaped article is a fiber mat.

Claim 17

The method of claim 6 wherein the shaped article is a fiber mat.

Claim 18

The method of claim 1 wherein from about 0.5 kilograms per square centimeter to about 2.5 kilograms per square centimeter of absolute pressure is applied to said shaped article during said heating to melt the boric acid.

Claim 19

The method of claim 6 wherein from about 0.5 kilograms per square centimeter to about 2.5 kilograms per square centimeter of absolute pressure is applied to said shaped article during said heating to melt the boric acid.

Claim 20

A shaped article manufactured in accordance with the method of claim 1.

Claim 21

A fiber mat manufactured in accordance with the method of claim 6.

Claim 24

The method of claim 21 wherein the boric acid is tetraboric acid.

Claim 25

The method of claim 21 wherein the boric acid is orthoboric acid.

Claim 26

The method of claim 21 wherein the boric acid is metaboric acid.

Claim 27

The method of claim 21 wherein the temperature above the melting temperature of the boric acid and below the melting or decomposition temperature of the boron oxide fiber is between about 160° C. to about 460° C.

Claim 28

The method of claim 25 wherein said sufficient time to melt the boric acid is from about three minutes to about three hours.

Claim 29

The method of claim 26 wherein said sufficient temperature to convert the boric acid and boron oxide fiber to boron nitride is from about 200° C. to about 900° C. and the sufficient time to convert the boric acid and boron oxide fiber is from about 2 to about 24 hours.

Claim 30

The method of claim 26 wherein the sufficient temperature to melt the boron oxide is from about 240° C. to about 265° C.

Claim 31

A flexible article manufactured in accordance with the method of claim 21.

Claim 32

A flexible article manufactured in accordance with the method of claim 26.

Claim 33

In an electric cell incorporating molten lithium chloride and a porous separator, the improvement wherein said separator comprises a flexible boron nitride fiber mat manufactured by: (a) blending from about 0.5 to about 40 weight percent of boric acid with from about 60 to about 99.5 weight percent of boron oxide fiber; (b) forming a shaped mat with the resulting blend; (c) heating the mat in an anhydrous gas selected from the group consisting of inert gases, nitrogen, ammonia and mixtures thereof to a temperature above the melting temperature of the boric acid and below about 265° C. for a time sufficient to melt at least some of the boric acid to the fibers; and (d) heating the mat in an ammonia atmosphere to a sufficient temperature and for a sufficient time to convert essentially all of the boric acid and boron oxide to boron nitride.

Claim 34

In an electric cell incorporating molten lithium chloride and a porous separator, the improvement wherein said separator comprises a flexible boron nitride fiber mat manufactured by: (a) blending from about 0.5 to about 40 weight percent of boric acid with from about 60 to about 99.5 weight percent of boron oxide fiber; (b) forming a shaped mat with the resulting blend; (c) heating the mat in an anhydrous gas selected from the group consisting of inert gases, nitrogen, ammonia and mixtures thereof to a temperature above the melting temperature of the boric acid and below about 265° C. for a time sufficient to melt at least some of the boric acid to the fibers; and (d) heating the mat in an ammonia atmosphere to a sufficient temperature and for a sufficient time to convert essentially all of the boric acid and boron oxide to boron nitride.

Claim 35

The electric cell of claim 31 wherein from about 2 to about 20 weight percent of boric acid is blended with from about 80 to about 98 weight percent of fiber.