Stratified particulate filter regeneration system

An exhaust gas treatment system for an internal combustion engine, comprising:

• an exhaust gas conduit in fluid communication with, and configured to receive an exhaust gas from the internal combustion engine;
• a hydrocarbon supply connected to and in fluid communication with the exhaust gas conduit, wherein the hydrocarbon supply is selectively adjustable for delivery of a hydrocarbon to control an exhaust gas temperature;
• a particulate filter (“PF”) device in fluid communication with the exhaust gas conduit and having a filter structure for removal of particulates in the exhaust gas, the filter structure having an innermost region, an outermost region, and a material limit that represents a maximum allowable temperature of the filter structure of the PF, the PF being selectively regenerated during operation of the internal combustion engine, the PF having a stratified temperature structure that causes the particulates trapped at the innermost region of the PF to burn off before the particulates trapped in the outermost region of the PF during regeneration, wherein the PF is regenerated within a regeneration time that represents an amount of time needed to complete regeneration of the PF;
• an oxidation catalyst device (“OC”) located upstream of the PF and in fluid communication with the exhaust gas conduit, wherein the OC device is selectively activated to induce oxidization of the exhaust gas;
• a pressure sensor in communication with the exhaust gas conduit, wherein the pressure sensor detects an operating condition of the PF, and wherein the pressure sensor generates a signal indicative of the amount of particulates trapped within the filter structure of the PF;
• a first temperature sensor and a second temperature sensor both in communication with the exhaust gas conduit, wherein the first temperature sensor is disposed upstream of the PF and the second temperature sensor is disposed downstream of the PF;
• and
• a control module in communication with the hydrocarbon supply, the pressure sensor, the first temperature sensor, and the second temperature sensor, the control module having a memory with an infinite stage temperature control curve stored therein, the temperature control curve indicating a temperature set point upstream of the PF, the temperature set point continuously changing to correspond to the amount of remaining particulates trapped within the filter structure of the PF during regeneration, wherein the temperature control curve is based on at least the stratified temperature structure of the PF, the particulates trapped in the innermost region of the PF, the particulates trapped in the outermost region of the PF, and the regeneration time of the PF, the control module comprising:
• a control logic for continuously monitoring the pressure sensor for the amount of particulates trapped within the filter structure of the PF and determining if the amount of particulates trapped within the filter structure exceed a threshold particulate value;
• a control logic for continuously monitoring the first temperature sensor for a first temperature reading and the second temperature sensor for a second temperature reading;
• a control logic for initiating regeneration of the PF if the amount of particulates trapped within the filter structure of the PF exceeds the threshold particulate value and if the first and second temperature readings exceed a threshold PF temperature;
• a control logic for correlating a temperature sensed from the first temperature sensor to the temperature set point of the temperature control curve, wherein the temperature set point of the temperature control curve is adjustable based on the amount of particulates trapped within the filter structure of the PF and the temperature at the first temperature sensor;
• and
• a control logic for continuously adjusting the hydrocarbon supply for delivery of hydrocarbons to control the exhaust gas temperature based on the temperature set point of the temperature control curve such that any point of the PF does not exceed the material limits of the filter structure of the PF.

An exhaust gas treatment system for an internal combustion engine, comprising:

• an exhaust gas conduit in fluid communication with, and configured to receive an exhaust gas from the internal combustion engine;
• a hydrocarbon supply connected to and in fluid communication with the exhaust gas conduit, wherein the hydrocarbon supply is selectively adjustable for delivery of a hydrocarbon to control an exhaust gas temperature;
• a particulate filter (“PF”) device in fluid communication with the exhaust gas conduit and having a filter structure for removal of particulates in the exhaust gas, the filter structure having an innermost region, a middle region, an outermost region, and a material limit that represents a maximum allowable temperature of the filter structure, the PF being selectively regenerated during operation of the internal combustion engine, the PF having a stratified temperature structure that causes the particulates trapped at the innermost region of the PF burn to off before the particulates trapped in the middle region of the PF, and the particulates trapped in the middle region of the PF burn off before the particulates trapped in the outermost region of the PF during regeneration, wherein the PF is regenerated within a regeneration time that represents an amount of time needed to complete regeneration of the PF;
• an oxidation catalyst device (“OC”) located upstream of the PF and in fluid communication with the exhaust gas conduit, wherein the OC device is selectively activated to induce oxidization of the exhaust gas;
• a pressure sensor in communication with the exhaust gas conduit, wherein the pressure sensor detects an operating condition of the PF, and wherein the pressure sensor generates a signal indicative of the amount of particulates trapped within the filter structure of the PF;
• a first temperature sensor and a second temperature sensor both in communication with the exhaust gas conduit, wherein the first temperature sensor is disposed upstream of the PF and the second temperature sensor is disposed downstream of the PF;
• and
• a control module in communication with the hydrocarbon supply, the pressure sensor, the first temperature sensor, and the second temperature sensor, the control module having a memory with an infinite stage temperature control curve stored therein, the temperature control curve indicating a temperature set point upstream of the PF, the temperature set point continuously changing to correspond to the amount of particulates trapped within the filter structure of the PF during regeneration, wherein the temperature control curve is based on at least the stratified temperature structure of the PF, test data, material properties of the filter structure of the PF, a particulate oxidization rate of the PF, an airflow rate into the PF, the particulates remaining trapped in the innermost region of the PF, the middle region of the PF, the particulates trapped in the outermost region of the PF, and the regeneration time of the PF, and wherein the test data is created by monitoring the PF in each of the innermost region, the middle region, and the outermost region of the PF, the control module comprising:
• a control logic for continuously monitoring the pressure sensor for the amount of particulates trapped within the filter structure of the PF and determining if the amount of particulates trapped within the filter structure exceed a threshold particulate value;
• a control logic for continuously monitoring the first temperature sensor for a first temperature reading and the second temperature sensor for a second temperature reading;
• a control logic for initiating regeneration of the PF if the amount of particulates trapped within the filter structure of the PF exceeds the threshold particulate value and if the first and second temperature readings exceed a threshold PF filter temperature;
• a control logic for correlating a temperature sensed from the first temperature sensor to the temperature set point of the temperature control curve, wherein the temperature set point of the temperature control curve is adjustable based on the amount of particulates trapped within the filter structure of the PF and the temperature at the first temperature sensor;
• and
• a control logic for continuously adjusting the hydrocarbon supply for delivery of hydrocarbons to control the exhaust gas temperature based on the temperature set point of the temperature control curve such that any point of the PF does not exceed the material limits of the filter structure of the PF.