Volatile organic compound abatement system

Claim 2

A volatile organic compound abatement system comprising: (a) at least one volatile organic compound adsorption unit; (b) supply means for inputting a desorption gas flow into said adsorption unit; (c) heat exchange means associated with said supply means for heating said desorption gas flow in said supply means; (d) transfer means for carrying a gas flow effluent from said adsorption unit; (e) a thermal regenerative oxidizing unit comprising a combustion chamber and a plurality of thermal regeneration beds, said unit connected to said transfer means to thereby receive said gas flow effluent in at least one of said regeneration beds; (f) bypass means coupled with said transfer means for allowing a predetermined portion of said gas flow effluent to circumvent said thermal regeneration beds and pass directly into said combustion chamber; (g) control means for sensing the temperature of said gas flow in said supply means and selectively activating said bypass means responsive to the temperature sensed; and (h) exhaust means coupled with said thermal regenerative oxidizing unit and associated with said heat exchange means for transferring thermal energy from the exhaust of said thermal regenerative oxidizing unit to said desorption gas flow prior to discharging said exhaust into the atmosphere.

Claim 3

The system according to claim 1 wherein said exhaust means further comprises a variable frequency drive fan for discharging the exhaust of the thermal regenerative oxidizing unit.

Claim 4

The system according to claim 2 wherein said transfer means further comprises pressure sensing means for maintaining constant pressure within said transfer means through controlling a variable fixed drive fan in response to a pressure drop across the system.

Claim 5

The system according to claim 1 wherein said supply means further comprises a heat exchange bypass means for selectively circumventing said heat exchange means.

Claim 6

The system according to claim 4 wherein said supply means further comprises a temperature sensing means placed at the input to said adsorption unit for selectively activating said heat exchange bypass means.

Claim 7

The system according to claim 1, wherein the control means comprises temperature sensing means attached to said supply means for selectively activating said bypass means to maintain a preselected desorption gas flow temperature.

Claim 8

A process for controlling the temperature of gases flowing through a volatile organic compound abatement system, in which a high temperature is consistently maintained in a combustion chamber and the thermal efficiency is selectively lowered in the combustion chamber in order to transfer thermal energy to other portions of the system, comprising the steps of: (a) introducing desorption gas to a heat exchanger; (b) sensing the temperature of the desorption gas; (c) transferring heated desorption gas from the heat exchanger to an adsorption unit to remove volatile organic compounds; (d) introducing effluent from the adsorption unit into a regenerative heating bed for heating gases prior to combustion; (e) directing said effluent from the regenerative heating bed to a combustion chamber; (f) selectively bypassing a predetermined amount of said gases around said regenerative heating bed and into said combustion chamber in response to said sensed temperature, in order to selectively lower the thermal efficiency of combustion and require excess thermal energy for oxidization; (g) oxidizing said effluent within the combustion chamber, thereafter discharging the combusted effluent from said chamber through another bed; (h) directing said oxidized effluent through said heat exchanger to transfer thermal energy to said desorption gases entering said adsorption unit; (i) disposing of said oxidized effluent.

Claim 9

A process for controlling the temperature of gases flowing through a volatile organic compound abatement system, in which a high temperature is consistently maintained in a combustion chamber and the thermal efficiency is selectively lowered in the combustion chamber in order to transfer thermal energy to other portions of the system, comprising the steps of: (a) introducing desorption gas to a heat exchanger; (b) sensing the temperature of the desorption gas; (c) transferring heated desorption gas from the heat exchanger to an adsorption unit to remove volatile organic compounds; (d) introducing effluent from the adsorption unit into a regenerative heating bed for heating gases prior to combustion; (e) directing said effluent from the regenerative heating bed to a combustion chamber; (f) selectively bypassing a predetermined amount of said gases around said regenerative heating bed and into said combustion chamber in response to said sensed temperature, in order to selectively lower the thermal efficiency of combustion and require excess thermal energy for oxidization; (g) oxidizing said effluent within the combustion chamber, thereafter discharging the combusted effluent from said chamber through another bed; (h) directing said oxidized effluent through said heat exchanger to transfer thermal energy to said desorption gases entering said adsorption unit; (i) disposing of said oxidized effluent.

Claim 10

The process of claim 7 further comprising sensing the pressure of effluent leaving an adsorption unit, said sensed pressure controlling the amount of work committed to disposing oxidized effluent so as to maintain a preselected pressure.