Exhaust emission purifier of internal combustion engine
US-9523300-B2 · Dec 20, 2016 · US
US10494975B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10494975-B2 |
| Application number | US-201816111333-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 24, 2018 |
| Priority date | Oct 11, 2017 |
| Publication date | Dec 3, 2019 |
| Grant date | Dec 3, 2019 |
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An ECU 30 calculates a target temperature of a bed temperature of a DOC 22 a under PM regeneration control at each control period by the elements M 1 to M 9 . Among these elements, the estimating section M 7 estimates a passing SO 3 amount at each control period by using an inflow SOx amount and a representative temperature. The estimating section M 8 estimates a SO 2 reduction rate, which is a ratio of reduction from SO 3 to SO 2 in the DOC 22 a . Then, the calculating unit M 9 calculates an amount of SO 3 that is allowed to desorb from the DOC 22 a as an allowable desorption SO 3 amount at each control period, by using a constrained SO 3 amount which corresponds to a constraint concerning sulfate white smoke, the passing SO 3 amount, and the SO 2 reduction rate.
Opening claim text (preview).
What is claimed is: 1. An engine control apparatus comprising: a purifying device provided in an exhaust pipe of a diesel engine; a fuel adding valve for supplying unburnt fuel into the purifying device; and an electronic control unit that executes temperature increase control of increasing a temperature of the purifying device to a target temperature in a temperature range in which a particulate matter burns by supplying unburnt fuel from the fuel adding valve, the electronic control unit is configured to: acquire a representative temperature that is a representative value of the purifying device at each predetermined control period; estimate an amount of SOx flowing into the purifying device as an inflow SOx amount at each control period; estimate a final adsorbed SOx distribution by using the inflow SOx amount and the representative temperature at each control period, the final adsorbed SOx distribution expressed as a graph in which an amount of SOx that finally adsorbs to the purifying device in each temperature during temperature increase of the purifying device is related with the representative temperature; estimate an amount of SOx that flows into the purifying device in a state of SOx and passes without adsorbing to the purifying device to be converted in a state of SO 3 as a passing SO 3 amount at each control period, by using the inflow SOx amount and the representative temperature; estimate a SO 2 reduction rate which is a ratio of reduction of SO 3 to SO 2 in the purifying device; calculate an amount of SO 3 that is allowed to desorb from the purifying device as an allowable desorption SO 3 amount at each control period, by using a constrained SO 3 amount at a downstream side of the purifying device, which corresponds to a constraint concerning sulfate white smoke, the passing SO 3 amount, and the SO 2 reduction rate; and calculate the target temperature at each control period, by using the final adsorbed SOx distribution and the allowable desorption SO 3 amount. 2. The engine control apparatus according to claim 1 , wherein the electronic control unit is configured to estimate the SO 2 reduction rate based on a relation between the SO 2 reduction rate, a supplied amount of unburnt fuel from the fuel adding valve, and a gas amount flowing into the purifying device. 3. The engine control apparatus according to claim 1 , wherein the electronic control unit is configured to: estimate a SOx saturation factor in the purifying device at each control period, by using an adsorbed SOx distribution expressed as a graph in which an amount of SOx that adsorbs to the purifying device in each temperature during temperature increase of the purifying device is related with the representative temperature of the purifying device and a saturation SOx distribution expressed as a graph in which an SOx maximum amount adsorbing to the purifying device in each temperature during temperature increase of the purifying device is related with the temperature of the purifying device; estimate an amount of SOx that flows into the purifying device and newly adsorbs to the purifying device as a newly adsorbing SOx amount at each control period by using the inflow SOx amount and the SOx saturation factor; estimate an amount of SOx that flows into the purifying device and passes without adsorbing to the purifying device as a passing SOx amount, by using the newly adsorbing SOx amount; and estimate the passing SO 3 amount at each control period, by using a conversion rate map expressing a relation between a conversion rate of SO 2 that is converted into SO 3 in the purifying device and the representative temperature. 4. The engine control apparatus according to claim 1 , wherein the electronic control unit is configured to: estimate an amount of SOx that newly desorbs from the purifying device as a newly desorbing SOx amount at each control period, by using the inflow SOx amount and the representative temperature; and estimate the final adsorbed SOx distribution at each control period, by using the newly desorbing SOx amount. 5. The engine control apparatus according to claim 1 , wherein the electronic control unit is configured to acquire a gas temperature at a downstream side of the purifying device as the representative temperature. 6. The engine control apparatus according to claim 1 , wherein the purifying device includes a filter that traps particulate matter flowing in the exhaust pipe, wherein the electronic control unit is configured to start the temperature increase control when an estimated value of an amount of particulate matter trapped by the filter reaches a removal request amount.
Exhaust gas temperature · CPC title
by means of filters · CPC title
Sulfur or sulfur oxides · CPC title
SOx amount trapped in catalyst · CPC title
with catalytic reactors · CPC title
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