Pulverized coal arc heated igniter system

Claim 2

Method of igniting pulverized coal suspended in an air stream comprising introducing an igniter gas selected from the group consisting of air, oxygen, mixtures of air and oxygen or mixtures of air or oxygen with other oxidizing, non-combustible or inert gases under pressure into a gas chamber having an exit nozzle, creating a vortex flow of said igniter gas through said gas chamber, establishing an electric arc between a pair of electrodes inside said gas chamber to heat the igniter gas to extremely high temperatures whereupon the gas emerges from said chamber through said exit nozzle in the form of a high velocity igniter gas jet composed predominantly of highly chemically active, ionized and dissociated species of said igniter gas, the temperature of said high velocity gas jet being in the range of from about 5,200° to about 15,000° F, and directing said igniter gas jet into contact with the pulverized coal-air stream to ignite the coal through spontaneous combustion.

Claim 3

The method in accordance with claim 1 wherein the hot high velocity igniter gas jet is maintained in contact with the pulverized coal-air stream after ignition occurs in order to stabilize the coal-air flame and prevent the flame from being extinguished.

Claim 4

The method in accordance with claim 1 wherein an auxiliary stream of preheated air is mixed with the pulverized coal-air stream.

Claim 5

Method of igniting pulverized coal in a coal burner wherein the pulverized coal is suspended in an air stream while passing through said coal burner, comprising introducing air under pressure into a gas chamber having an exit nozzle, establishing an electric arc from a high voltage power supply between a pair of electrodes to heat the air introduced into said chamber to extremely high temperatures whereupon the heated air emerges from said chamber through said exit nozzle in the form of a hot high velocity air jet, and directing the hot high velocity air jet into contact with the pulverized coal-air stream while maintaining the flow rate of both the pulverized coal and air stream, the power in the hot high velocity air jet and the bulk total enthalpy thereof at predetermined values such that the dimensionless parameter "f" in the following equation equals or exceeds a minimum value within the range of between about 0.70 and 0.80 ##EQU2## where P gas = the power in the hot high velocity air jet expressed in kilowatts h = the bulk total enthalpy of the hot high velocity air jet expressed in BTU per pound w pa = the air flow rate through said coal burner expressed in pounds per second w c = the coal flow rate through said coal burner expressed in pounds per second.

Claim 6

Method of igniting pulverized coal in a coal burner wherein the pulverized coal is suspended in an air stream while passing through said coal burner, comprising introducing air under pressure into a gas chamber having an exit nozzle, establishing an electric arc from a high voltage power supply between a pair of electrodes to heat the air introduced into said chamber to extremely high temperatures whereupon the heated air emerges from said chamber through said exit nozzle in the form of a hot high velocity air jet, and directing the hot high velocity air jet into contact with the pulverized coal-air stream while maintaining the flow rate of both the pulverized coal and air stream, the power in the hot high velocity air jet and the bulk total enthalpy thereof at predetermined values such that the dimensionless parameter "f" in the following equation equals or exceeds a minimum value within the range of between about 0.70 and 0.80 ##EQU2## where P gas = the power in the hot high velocity air jet expressed in kilowatts h = the bulk total enthalpy of the hot high velocity air jet expressed in BTU per pound w pa = the air flow rate through said coal burner expressed in pounds per second w c = the coal flow rate through said coal burner expressed in pounds per second.