Carbon black

Claim 2

An oxygenated furnace carbon black having a particle size of at least 15 millimicrons, a dibutylphthalate absorption value not exceeding 120 c.c./100 gms, a nitrogen surface area of at least 450 m 2 /gm., and an oxygen content of at least 4 weight percent.

Claim 3

Furnace carbon black as in claim 1 having a volatile content of at least 6 weight percent.

Claim 4

An oxygenated furnace carbon black having a particle size within the range of 15 to 60 millimicrons, a dibutylphthalate absorption within the range of 60-120 c.c./100 gms., a nitrogen surface area within the range of 450 to 1000 m 2 /gm., and an oxygen content of 4 to 10 weight percent.

Claim 5

An oxygenated furnace carbon black having a particle size within the range of 15 to 60 millimicrons, a dibutylphthalate absorption within the range of 60-120 c.c./100 gms., a nitrogen surface area within the range of 450 to 1000 m 2 /gm., and an oxygen content of 4 to 10 weight percent.

Claim 6

A furnace carbon black as in claim 3 having a volatile content of 6.5 to 16.5 weight percent.

Claim 7

An oxygenated furnace carbon black having a particle size of about 25 to about 50 millimicrons, a dibutylphthalate absorption of about 80 to about 120 c.c./100 gms., a nitrogen surface area of about 500 to about 700 m 2 /gm., and an oxygen content of about 5 to about 8 weight percent.

Claim 8

An oxygenated furnace carbon black having a particle size of about 25 to about 50 millimicrons, a dibutylphthalate absorption of about 80 to about 120 c.c./100 gms., a nitrogen surface area of about 500 to about 700 m 2 /gm., and an oxygen content of about 5 to about 8 weight percent.

Claim 9

A furnace carbon black as in claim 5 having a volatile content of about 7 to about 13.5 weight percent.

Claim 10

An oxygenated furnace carbon black having a particle size of about 25 to about 35 millimicrons, a dibutylphthalate absorption of about 100 to about 120 c.c./100 gms., a nitrogen surface area of about 500 to about 600 m 2 /gm., and an oxygen content of about 5 to about 7 weight percent.

Claim 11

An oxygenated furnace carbon black having a particle size of about 25 to about 35 millimicrons, a dibutylphthalate absorption of about 100 to about 120 c.c./100 gms., a nitrogen surface area of about 500 to about 600 m 2 /gm., and an oxygen content of about 5 to about 7 weight percent.

Claim 12

A furnace carbon black as in claim 7 having a volatile content of about 7 to about 10.5 weight percent.

Claim 13

An oxygenated furnace carbon black having a particle size of about 30 millimicrons, a dibutylphthalate absorption of about 100 c.c./100 gms., a nitrogen surface area of about 500 m 2 /gm., and an oxygen content of about 6 weight percent.

Claim 14

An oxygenated furnace carbon black having a particle size of about 30 millimicrons, a dibutylphthalate absorption of about 100 c.c./100 gms., a nitrogen surface area of about 500 m 2 /gm., and an oxygen content of about 6 weight percent.

Claim 15

A furnace carbon black as in claim 9 having a volatile content of about 9.5 weight percent.

Claim 16

Method of producing a carbon black having a high surface area and a high oxygen content which comprises reacting an oxidizing agent with a previously unoxidized furnace carbon black which is characterized by: a. a particle size of at least 15 millimicrons, b. a dibutylphthalate absorption of no greater than 120 c.c/100 gms., c. a nitrogen surface area of at least 500 m 2 /gm., d. a volatile content no greater than about 3 weight percent and wherein following the reaction of said oxidizing agent with said carbon black an oxygenated carbon black product is recovered that has a nitrogen surface area of at least 450 m 2 /gm., an oxygen content of at least 4 weight percent, and a dibutylphthalate absorption of no less than about 60 c.c./100 gms.

Claim 17

Method of producing a carbon black having a high surface area and a high oxygen content which comprises reacting an oxidizing agent with a previously unoxidized furnace carbon black which is characterized by: a. a particle size of at least 15 millimicrons, b. a dibutylphthalate absorption of no greater than 120 c.c/100 gms., c. a nitrogen surface area of at least 500 m 2 /gm., d. a volatile content no greater than about 3 weight percent and wherein following the reaction of said oxidizing agent with said carbon black an oxygenated carbon black product is recovered that has a nitrogen surface area of at least 450 m 2 /gm., an oxygen content of at least 4 weight percent, and a dibutylphthalate absorption of no less than about 60 c.c./100 gms.

Claim 18

A method as in claim 11 wherein the increased oxygen content of the recovered carbon black is oxygen derived through contact of the carbon black with ozone.

Claim 19

A method as defined in claim 11 wherein the increased oxygen content of the recovered carbon black is oxygen derived through contact of the carbon black with N x O y where x is from 1 to 2 and y is from 1 to 4.

Claim 20

A method as in claim 13 wherein the carbon black is first mixed with nitric acid and is then heated to liberate N x O y .

Claim 21

A method as in claim 14 wherein the mixture of carbon black and nitric acid is heated at a temperature within the range of about 250°-300°F.

Claim 22

A method as in claim 14 wherein the ratio of carbon black and nitric acid, on a water-free basis, is about 1/1.

Claim 23

A method as in claim 14 wherein the nitric acid is in the form of an aqueous solution thereof wherein the concentration of nitric acid is at least about 50 weight percent.

Claim 24

A method as in claim 11 wherein the volatile content of the carbon black, prior to said combining with oxygen does not exceed about 2 weight percent and is at least about 6 weight percent following said combining with oxygen.

Claim 25

In a process wherein a carbon black is mixed with an aqueous solution of nitric acid for oxygenation of the black, and the resulting mixture is heated to drive off water and release one or more N x O y compounds, the method for accelerated oxygenation and drying of the carbon black while perserving the surface area and maximizing oxygen content thereof which comprises passing said mixture through a first enclosed heating zone and then through a second enclosed heating zone that is in open communication with the first, introducing heat into both of said zones but at a higher rate into said first zone than into said second zone, the input of heat into said first zone being maintained at a rate which results in discharge of dried carbon black from said second zone which is at a temperature within the range of about 250°F. to about 300°F., and wherein gases and vapors which result from heating of said mixture flow in a direction which is concurrent with respect to passage of the carbon black through said zones for contact with said black prior to the discharge thereof from said second zone.

Claim 26

In a process wherein a carbon black is mixed with an aqueous solution of nitric acid for oxygenation of the black, and the resulting mixture is heated to drive off water and release one or more N x O y compounds, the method for accelerated oxygenation and drying of the carbon black while perserving the surface area and maximizing oxygen content thereof which comprises passing said mixture through a first enclosed heating zone and then through a second enclosed heating zone that is in open communication with the first, introducing heat into both of said zones but at a higher rate into said first zone than into said second zone, the input of heat into said first zone being maintained at a rate which results in discharge of dried carbon black from said second zone which is at a temperature within the range of about 250°F. to about 300°F., and wherein gases and vapors which result from heating of said mixture flow in a direction which is concurrent with respect to passage of the carbon black through said zones for contact with said black prior to the discharge thereof from said second zone.

Claim 27

A process as in claim 19 wherein the carbon black that is mixed with the nitric acid is characterized by: a. a particle size of at least 15 millimicrons, b. a dibutylphthalate absorption of no greater than 120 c.c./100 gms., c. a nitrogen surface area of at least 500 m 2 /gm., d. a volatile content no greater than about 3 weight percent, and wherein the dried oxygenated carbon black product that is recovered has a nitrogen surface area of at least 450 m 2 /gm., an oxygen content of at least 4 weight percent, and a dibutylphthalate absorption of no less than about 60 c.c./100 gms.

Claim 28

A process as in claim 19 wherein the carbon black is dried to a moisture content (ASTM D1509-59) of not exceeding about 2.5 weight percent.