Production of high structure soft carbon black

Claim 1

A method of producing a high structure soft carbon black which comprises: a. introducing a liquid hydrocarbon feed into a first zone of a tubular reactor; b. tangentially introducing hot combustion gases being produced by the oxidation of a gaseous fuel with air employing an air to fuel volume ratio or about 16 to 1 into said first zone, c. forming a mixture of said liquid hydrocarbon feed and said hot combustion gases in said first zone to bring said hydrocarbon feed to its pyrolytic decomposition temperature, employing an air total to liquid hydrocarbon feed ratio of about 340 to about 360 SCF per gallon, d. passing said mixture through said first zone at a first velocity while increasing the temperature of said liquid hydrocarbon feed to its pyrolytic decomposition temperature, e. upon attainment of the hydrocarbon feed of its pyrolytic decomposition temperature passing said mixture into a second zone while continuing the pyrolytic decomposition of said liquid hydrocarbon feed, f. passing said mixture through said second zone at a second velocity of about 20 to about 30 feet/second to form carbon black, said first velocity being about 2.5 to about 3 times the second velocity, and g. recovering said carbon black.

Claim 2

A method of producing a high structure soft carbon black which comprises: a. introducing a liquid hydrocarbon feed into a first zone of a tubular reactor; b. tangentially introducing hot combustion gases being produced by the oxidation of a gaseous fuel with air employing an air to fuel volume ratio or about 16 to 1 into said first zone, c. forming a mixture of said liquid hydrocarbon feed and said hot combustion gases in said first zone to bring said hydrocarbon feed to its pyrolytic decomposition temperature, employing an air total to liquid hydrocarbon feed ratio of about 340 to about 360 SCF per gallon, d. passing said mixture through said first zone at a first velocity while increasing the temperature of said liquid hydrocarbon feed to its pyrolytic decomposition temperature, e. upon attainment of the hydrocarbon feed of its pyrolytic decomposition temperature passing said mixture into a second zone while continuing the pyrolytic decomposition of said liquid hydrocarbon feed, f. passing said mixture through said second zone at a second velocity of about 20 to about 30 feet/second to form carbon black, said first velocity being about 2.5 to about 3 times the second velocity, and g. recovering said carbon black.