Non-carcinogenic carbon black

Claim 2

A process for the production of a non-carcinogenic carbon black comprising a. pyrolytically in a carbon black furnace decomposing a hydrocarbon feedstock having a low carbon residue of less than about 0.2 weight % such as to form a smoke containing a carbon black having a CTAB surface area of about 80 m 2 /g or more, b. aftertreating said smoke by subjecting it to at least one of the steps of late quenching and secondary air injecting such as to produce a smoke containing a carbon black having a photelometer of about 100% and a pitting degree defined as the difference between the nitrogen surface area and the CTAB surface area of 7 m 2 /g or more, c. oxidizing the carbon black and pelleting the carbon black with an aqueous pelleting agent, and d. drying the wet carbon black pellets at a temperature of about 500° to 600° F.

Claim 3

A process in accordance with claim 1 wherein said feedstock is selected from the group consisting of toluene and SO 2 extract oil.

Claim 4

A process in accordance with claim 1 wherein said carbon black is oxidized by contacting the carbon black with an aqueous solution of HNO 3 so that the mixture of carbon black and aqueous pelleting agent contains about 2 to 10 wt. % of HNO 3 based on the carbon black as 100%.

Claim 5

A process in accordance with claim 1 wherein said aftertreating of said carbon black containing smoke is carried out by a late quench step and/or by the introduction of secondary air between the main carbon black forming reaction zone and a quench location.

Claim 6

A non-carcinogenic carbon black obtained by a pyrolytic decomposition in a carbon black furnace of a hydrocarbon feedstock having a carbon residue of less than about 0.2 weight percent into a carbon black containing smoke, aftertreating said carbon black containing smoke by subjecting it to at least one of the steps of late quenching and secondary air injecting, oxidizing the so-produced carbon black and pelleting the carbon black with an aqueous pelleting agent and drying the wet carbon black pellets at a temperature of about 500° to 600° F., said carbon black being further characterized by having a CTAB surface area of 80 m 2 /g or more a pitting degree of 7 m 2 /g or more, said pitting degree being defined as the difference between the nitrogen surface area in the CTAB surface area, a photelometer of 100 percent, and a content of benzene extractables of less than 0.05 weight percent.

Claim 7

A non-carcinogenic carbon black obtained by a pyrolytic decomposition in a carbon black furnace of a hydrocarbon feedstock having a carbon residue of less than about 0.2 weight percent into a carbon black containing smoke, aftertreating said carbon black containing smoke by subjecting it to at least one of the steps of late quenching and secondary air injecting, oxidizing the so-produced carbon black and pelleting the carbon black with an aqueous pelleting agent and drying the wet carbon black pellets at a temperature of about 500° to 600° F., said carbon black being further characterized by having a CTAB surface area of 80 m 2 /g or more a pitting degree of 7 m 2 /g or more, said pitting degree being defined as the difference between the nitrogen surface area in the CTAB surface area, a photelometer of 100 percent, and a content of benzene extractables of less than 0.05 weight percent.

Claim 8

A polymer composition consisting essentially of 100 parts by weight of a polymer selected from the group of rubbers and thermoplastic polymers and about 1 to about 200 parts by weight of carbon black of claim 5 per 100 parts by weight of rubber and 0.1 to 50 parts by weight of carbon black of claim 5 per 100 parts by weight of thermoplastic polymer.

Claim 9

A polymer composition in accordance with claim 5 containing about 20 to 80 parts by weight of said carbon black per 100 parts by weight of rubber.

Claim 10

A polymer composition in accordance with claim 6 consisting essentially of 100 parts by weight of a thermoplastic polymer and 0.1 to 10 parts by weight of a carbon black produced in accordance with claim 1.