U.S. patent application number 12/227718 was filed with the patent office on 2009-10-08 for exhaust purification system of internal combustion engine.
This patent application is currently assigned to TOYOTA JIDOSHA KABUSHIKI KAISHA. Invention is credited to Takamitsu Asanuma, Atsushi Hayashi, Kotaro Hayashi, Shinya Hirota, Kohei Yoshida.
Application Number | 20090249768 12/227718 |
Document ID | / |
Family ID | 38845701 |
Filed Date | 2009-10-08 |
United States Patent
Application |
20090249768 |
Kind Code |
A1 |
Asanuma; Takamitsu ; et
al. |
October 8, 2009 |
Exhaust Purification System of Internal Combustion Engine
Abstract
HC feed control for feeding HC into exhaust gas upstream of an
SOx trap 11 when a predetermined condition stands is executed. When
an SOx trap amount is smaller than a predetermined amount, as HC
feed control, first HC feed control feeding HC into the exhaust gas
upstream of the SOx trap by a predetermined pattern is executed.
When the SOx trap amount is larger than a predetermined amount, as
HC feed control, second HC feed control feeding HC into the exhaust
gas upstream of the SOx trap by a pattern different from the
predetermined pattern, which pattern keeping the temperature of the
SOx trap from locally becoming higher than the predetermined
temperature or suppressing the formation of a region in the exhaust
gas flowing into the SOx trap where the air-fuel ratio becomes
locally rich, is executed.
Inventors: |
Asanuma; Takamitsu;
(Mishima-shi, JP) ; Hirota; Shinya; (Susono-shi,
JP) ; Hayashi; Kotaro; (Mishima-shi, JP) ;
Yoshida; Kohei; (Gotenba-shi, JP) ; Hayashi;
Atsushi; (Susono-shi, JP) |
Correspondence
Address: |
OLIFF & BERRIDGE, PLC
P.O. BOX 320850
ALEXANDRIA
VA
22320-4850
US
|
Assignee: |
TOYOTA JIDOSHA KABUSHIKI
KAISHA
Toyota-shi
JP
|
Family ID: |
38845701 |
Appl. No.: |
12/227718 |
Filed: |
June 29, 2007 |
PCT Filed: |
June 29, 2007 |
PCT NO: |
PCT/JP2007/063508 |
371 Date: |
November 25, 2008 |
Current U.S.
Class: |
60/286 ;
60/299 |
Current CPC
Class: |
B01D 2257/302 20130101;
F01N 3/085 20130101; F02D 41/0285 20130101; Y02T 10/47 20130101;
F01N 3/0814 20130101; Y02T 10/40 20130101; B01D 53/9409 20130101;
F01N 3/106 20130101; Y02A 50/20 20180101; F02D 41/405 20130101;
F01N 3/0885 20130101; B01D 53/9495 20130101; B01D 2251/208
20130101; B01D 53/90 20130101; F01N 3/0871 20130101; F01N 13/009
20140601; F01N 9/002 20130101; Y02A 50/2348 20180101; Y02T 10/44
20130101; F01N 2900/1612 20130101; F02B 37/00 20130101; F01N
2610/03 20130101; F01N 3/0842 20130101 |
Class at
Publication: |
60/286 ;
60/299 |
International
Class: |
F01N 9/00 20060101
F01N009/00; F01N 3/10 20060101 F01N003/10 |
Foreign Application Data
Date |
Code |
Application Number |
Jun 30, 2006 |
JP |
2006-181380 |
Claims
1. An exhaust purification system of an internal combustion engine
providing an SOx trap for trapping the SOx in the exhaust gas
inside an exhaust passage, said SOx trap trapping the SOx in the
exhaust gas when an air-fuel ratio of the exhaust gas flowing into
said SOx trap is an air-fuel ratio leaner than a stoichiometric
air-fuel ratio and a temperature of said SOx trap is lower than a
predetermined temperature and releasing the trapped SOx when the
air-fuel ratio of the exhaust gas flowing into said SOx trap is the
stoichiometric air-fuel ratio or an air-fuel ratio richer than that
and the temperature of said SOx trap is higher than said
predetermined temperature and executing HC feed control feeding HC
into the exhaust gas upstream of the SOx trap when a predetermined
condition stands, said exhaust purification system of an internal
combustion engine executes, as said HC feed control, first HC feed
control feeding HC into the exhaust gas upstream of the SOx trap by
a predetermined pattern when the amount of SOx which the SOx trap
traps is smaller than a predetermined amount and executes, as said
HC feed control, second HC feed control feeding HC into the exhaust
gas upstream of the SOx trap by a pattern different from said
predetermined pattern, which pattern keeping the temperature of the
SOx trap from locally becoming higher than said predetermined
temperature or suppressing the formation of a region in the exhaust
gas flowing into the SOx trap where the air-fuel ratio becomes
locally rich, when the amount of SOx which the SOx trap traps is
larger than said predetermined amount.
2. An exhaust purification system of an internal combustion engine
as set forth in claim 1, wherein, in said first HC feed control, a
predetermined amount of HC is fed into the exhaust gas upstream of
the SOx trap per unit time, while in said second HC feed control,
an amount of HC smaller than said predetermined amount is fed into
the exhaust gas upstream of the SOx trap per unit time.
3. An exhaust purification system of an internal combustion engine
as set forth in claim 1, wherein, in said second HC feed control,
HC with a higher diffusion ability into the exhaust gas than the HC
fed into the exhaust gas upstream of the SOx trap in said first HC
feed control is fed into the exhaust gas upstream of the SOx
trap.
4. An exhaust purification system of an internal combustion engine
as set forth in claim 2, wherein, in said second HC feed control,
HC is fed into the exhaust gas upstream of the SOx trap so that a
lean degree of the air-fuel ratio of the exhaust gas flowing into
the SOx trap is kept larger than a predetermined lean degree.
5. An exhaust purification system of an internal combustion engine
as set forth in claim 3, wherein, in said second HC feed control,
HC is fed into the exhaust gas upstream of the SOx trap so that a
lean degree of the air-fuel ratio of the exhaust gas flowing into
the SOx trap is kept larger than a predetermined lean degree.
6. An exhaust purification system of an internal combustion engine
as set forth in claim 4, wherein said predetermined lean degree is
set larger the lower the temperature of the SOx trap.
7. An exhaust purification system of an internal combustion engine
as set forth in claim 5, wherein said predetermined lean degree is
set larger the lower the temperature of the SOx trap.
8. An exhaust purification system of an internal combustion engine
as set forth in claim 1, wherein, in said second HC feed control,
HC is fed into the exhaust gas upstream of the SOx trap so that the
amount of local temperature rise of the SOx trap per unit time is
kept smaller than the amount of local temperature rise of the SOx
trap per unit time allowed in said first HC feed control.
9. An exhaust purification system of an internal combustion engine
as set forth in claim 8, wherein, in said second HC feed control,
HC is fed into the exhaust gas upstream of the SOx trap so that an
amount of temperature rise of the SOx trap as a whole per unit time
is kept smaller than an amount of temperature rise of the SOx trap
as a whole per unit time allowed in said first HC feed control.
10. An exhaust purification system of an internal combustion engine
as set forth in claim 8, wherein a particulate filter trapping
particulate matter in the exhaust gas is arranged in the exhaust
passage downstream of said SOx trap, one said predetermined
condition is a burnaway condition where it is judged if the
temperature of said particulate filter should be raised to a
predetermined target temperature to burn away particulate matter
trapped by the particulate filter, and, when said second HC feed
control is executed when said burnaway condition stands, in said
second HC feed control, HC is fed into the exhaust gas upstream of
the SOx trap using as a target temperature a temperature lower than
said target temperature in said first HC feed control in the case
where said first HC feed control is executed when said burnaway
condition stands.
11. An exhaust purification system of an internal combustion engine
as set forth in claim 9, wherein, in said second HC feed control,
HC is fed into the exhaust gas upstream of the SOx trap so that a
temperature amplitude of the SOx is kept smaller than a temperature
amplitude of the SOx trap allowed in said first HC feed
control.
12. An exhaust purification system of an internal combustion engine
as set forth in claim 10, wherein, in said second HC feed control,
HC is fed into the exhaust gas upstream of the SOx trap so that a
temperature amplitude of the SOx is kept smaller than a temperature
amplitude of the SOx trap allowed in said first HC feed
control.
13. An exhaust purification system of an internal combustion engine
as set forth in claim 8, wherein, an NOx absorbent absorbing the
NOx in the exhaust gas is arranged in the exhaust passage
downstream of said SOx trap, one said predetermined condition is an
NOx release condition where it is judged that said NOx absorbent
should release NOx, and, when said second HC feed control is
executed when said NOx release condition stands, in said second HC
feed control, HC is fed into the exhaust gas upstream of the SOx
trap so that a temperature amplitude of the SOx trap is kept
smaller than a temperature amplitude of the SOx trap allowed in
said first HC feed control in the case where said first HC feed
control is executed when said NOx release condition stands.
14. An exhaust purification system of an internal combustion engine
as set forth in claim 1, wherein an oxidation catalyst provided
with an oxidizing ability higher than even the oxidizing ability of
said SOx trap is arranged in the exhaust passage upstream of said
SOx trap.
Description
TECHNICAL FIELD
[0001] The present invention relates to an exhaust purification
system of an internal combustion engine.
BACKGROUND ART
[0002] Japanese Patent Publication (A) No. 6-173652 describes an
internal combustion engine providing an exhaust purification system
absorbing NOx (nitrogen oxides) in the exhaust gas in an exhaust
passage. Here, the exhaust gas also contains SOx. The NOx absorbent
described in Japanese Patent Publication (A) No. 6-173652 absorbs
SOx in addition to NOx so the amount of NOx which the NOx absorbent
can absorb ends up being reduced by exactly the amount of
absorption of SOx. Thus, in the exhaust purification system
described in Japanese Patent Publication (A) No. 6-173652, an SOx
absorbent for absorbing SOx in the exhaust gas is arranged upstream
of the NOx absorbent and the SOx absorbent is used to absorb the
SOx in the exhaust gas and prevent SOx from flowing into the NOx
absorbent.
DISCLOSURE OF THE INVENTION
[0003] In this regard, in general, an SOx absorbent absorbs the SOx
in the exhaust gas when the air-fuel ratio of the exhaust gas
flowing into it is an air-fuel ratio leaner than the stoichiometric
air-fuel ratio and the temperature of the SOx absorbent is higher
than a so-called activation temperature. On the other hand, the SOx
absorbent releases SOx when the air-fuel ratio of the exhaust gas
flowing into it becomes the stoichiometric air-fuel ratio or an
air-fuel ratio richer than that and the temperature of the SOx
absorbent becomes higher than a certain temperature higher than the
activation temperature (hereinafter referred to as the "SOx release
temperature"). Here, the SOx absorbent has the absorption of SOx in
the exhaust gas as its inherent function, so when the SOx absorbent
should be made to absorb SOx, it is not preferable that the SOx
absorbent end up releasing SOx. Further, this applies not only to
an exhaust purification system provided with an SOx absorbent for
the purpose of absorbing the SOx in the exhaust gas, but also
broadly to an exhaust purification system provided with an SOx trap
for the purpose of trapping the SOx in the exhaust gas.
[0004] An object of the present invention is to reliably prevent an
SOx trap from ending up releasing SOx when the SOx trap should be
made to trap SOx in an internal combustion engine provided with an
SOx trap trapping the SOx in the exhaust gas.
[0005] To solve the problem, in a first aspect of the present
invention, there is provided an exhaust purification system of an
internal combustion engine providing an SOx trap for trapping the
SOx in the exhaust gas inside an exhaust passage, the SOx trap
trapping the SOx in the exhaust gas when an air-fuel ratio of the
exhaust gas flowing into the SOx trap is an air-fuel ratio leaner
than a stoichiometric air-fuel ratio and a temperature of the SOx
trap is lower than a predetermined temperature and releasing the
trapped SOx when the air-fuel ratio of the exhaust gas flowing into
the SOx trap is the stoichiometric air-fuel ratio or an air-fuel
ratio richer than that and the temperature of the SOx trap is
higher than the predetermined temperature and executing HC feed
control feeding HC into the exhaust gas upstream of the SOx trap
when a predetermined condition stands, which exhaust purification
system of an internal combustion engine executes, as the HC feed
control, first HC feed control feeding HC into the exhaust gas
upstream of the SOx trap by a predetermined pattern when the amount
of SOx which the SOx trap traps is smaller than a predetermined
amount and executes, as the HC feed control, second HC feed control
feeding HC into the exhaust gas upstream of the SOx trap by a
pattern different from the predetermined pattern, which pattern
keeping the temperature of the SOx trap from locally becoming
higher than the predetermined temperature or suppressing the
formation of a region in the exhaust gas flowing into the SOx trap
where the air-fuel ratio becomes locally rich, when the amount of
SOx which the SOx trap traps is larger than the predetermined
amount.
[0006] In a second aspect of the present invention, in the first HC
feed control, a predetermined amount of HC is fed into the exhaust
gas upstream of the SOx trap per unit time, while in the second HC
feed control, an amount of HC smaller than the predetermined amount
is fed into the exhaust gas upstream of the SOx trap per unit
time.
[0007] In a third aspect of the present invention, in the second HC
feed control, HC with a higher diffusion ability into the exhaust
gas than the HC fed into the exhaust gas upstream of the SOx trap
in the first HC feed control is fed into the exhaust gas upstream
of the SOx trap.
[0008] In a fourth aspect of the present invention, in the second
HC feed control, HC is fed into the exhaust gas upstream of the SOx
trap so that a lean degree of the air-fuel ratio of the exhaust gas
flowing into the SOx trap is kept larger than a predetermined lean
degree.
[0009] In a fifth aspect of the present invention, the
predetermined lean degree is set larger the lower the temperature
of the SOx trap.
[0010] In a sixth aspect of the present invention, in the second HC
feed control, HC is fed into the exhaust gas upstream of the SOx
trap so that the amount of local temperature rise of the SOx trap
per unit time is kept smaller than the amount of local temperature
rise of the SOx trap per unit time allowed in the first HC feed
control.
[0011] In a seventh aspect of the present invention, in the second
HC feed control, HC is fed into the exhaust gas upstream of the SOx
trap so that an amount of temperature rise of the SOx trap as a
whole per unit time is kept smaller than an amount of temperature
rise of the SOx trap as a whole per unit time allowed in the first
HC feed control.
[0012] In an eighth aspect of the present invention, a particulate
filter trapping particulate matter in the exhaust gas is arranged
in the exhaust passage downstream of the SOx trap, one
predetermined condition is a fuel removal condition where it is
judged if the temperature of the particulate filter should be
raised to a predetermined target temperature to burn away
particulate matter trapped by the particulate filter, and, when the
second HC feed control is executed when the burnaway condition
stands, in the second HC feed control, HC is fed into the exhaust
gas upstream of the SOx trap using as a target temperature a
temperature lower than the target temperature in the first HC feed
control in the case where the first HC feed control is executed
when the burnaway condition stands.
[0013] In a ninth aspect of the present invention, in the second HC
feed control, HC is fed into the exhaust gas upstream of the SOx
trap so that a temperature amplitude of the SOx is kept smaller
than a temperature amplitude of the SOx trap allowed in the first
HC feed control.
[0014] In a 10th aspect of the present invention, an NOx absorbent
absorbing the NOx in the exhaust gas is arranged in the exhaust
passage downstream of the SOx trap, one predetermined condition is
an NOx release condition where it is judged that the NOx absorbent
should release NOx, and, when the second HC feed control is
executed when the NOx release condition stands, in the second HC
feed control, HC is fed into the exhaust gas upstream of the SOx
trap so that a temperature amplitude of the SOx trap is kept
smaller than a temperature amplitude of the SOx trap allowed in the
first HC feed control in the case where the first HC feed control
is executed when the NOx release condition stands.
[0015] In an 11th aspect of the present invention, an oxidation
catalyst provided with an oxidizing ability higher than even the
oxidizing ability of the SOx trap is arranged in the exhaust
passage upstream of the SOx trap.
[0016] Below, the present invention will be able to be understood
more clearly from the attached drawings and the description of
preferred embodiments of the present invention.
BRIEF DESCRIPTION OF THE DRAWINGS
[0017] FIG. 1 is a view showing a compression ignition type of
internal combustion engine provided with an exhaust purification
system of the present invention.
[0018] FIGS. 2(A) and (B) are views showing the structure of a
particulate filter.
[0019] FIG. 3 is a cross-sectional view of a surface part of a
catalyst carrier of an NOx catalyst.
[0020] FIG. 4 is a cross-sectional view of a surface part of a
catalyst carrier of an SOx trap.
[0021] FIGS. 5(A) to (C) are views for explaining NOx release
control of an exhaust purification system of a first
embodiment.
[0022] FIGS. 6(A) to (C) is a view for explaining NOx release
control of an exhaust purification system of a second
embodiment.
[0023] FIG. 7 is a view showing an example of a routine for
executing NOx release control of an embodiment of the present
invention.
[0024] FIGS. 8(A) to (C) are views for explaining the PM removal
control of the exhaust purification system of a seventh
embodiment.
[0025] FIGS. 9(A) to (C) are views for explaining the PM removal
control of the exhaust purification system of an eighth
embodiment.
[0026] FIG. 10 is a view showing an example of a routine for
executing PM removal control of an embodiment of the present
invention.
[0027] FIG. 11 is a view showing an example of a routine for
executing NOx release control of an exhaust purification system of
a 15th embodiment.
[0028] FIG. 12 is a view showing an example of a routine for
executing PM removal control of an exhaust purification system of a
16th embodiment.
[0029] FIG. 13 is a view showing one of the compression ignition
type of internal combustion engine to which the present invention
can be applied.
[0030] FIG. 14 is a view showing another one of the compression
ignition type of internal combustion engine to which the present
invention can be applied.
[0031] FIG. 15 is a view showing still another one of the
compression ignition type of internal combustion engine to which
the present invention can be applied.
BEST MODE FOR CARRYING OUT THE INVENTION
[0032] Below, an embodiment of the present invention will be
explained with reference to the drawings. FIG. 1 shows a
compression ignition type of internal combustion engine provided
with an exhaust purification system of the present invention. In
FIG. 1, 1 shows an engine body, 2 a combustion chamber of each
cylinder, 3 an electronic control type fuel injector for injecting
fuel into each combustion chamber 2, 4 an intake manifold, and 5 an
exhaust manifold. The intake manifold 4 is connected through an
intake duct 6 to an outlet of a compressor 7a of an exhaust
turbocharger 7, while an inlet of the compressor 7a is connected to
an air cleaner 8. Inside the intake duct 6 is arranged a throttle
valve 9 driven by a step motor. Further, around the intake duct 6
is arranged a cooling device 10 for cooling the intake air flowing
inside the intake duct 6. In the embodiment shown in FIG. 1, the
engine cooling water is guided into the cooling device 10 where the
engine cooling water is used to cool the intake air. On the other
hand, the exhaust manifold 5 is connected to the inlet of the
exhaust turbine 7b of the exhaust turbocharger 7, while the outlet
of the exhaust turbine 7b is connected through an exhaust pipe 13
to the inlet of the SO.sub.x trap 11. The exhaust pipe 13 has
attached to it an HC (hydrocarbon) feed valve 14 for feeding for
example HC in the exhaust gas flowing through the inside of the
exhaust pipe 13. Further, the outlet of the SOx trap 11 is
connected to the NOx catalyst 12.
[0033] The exhaust manifold 5 and the intake manifold 4 are
connected to each other through an exhaust gas recirculation
(hereinafter referred to as the "EGR") passage 15. Inside the EGR
passage 15 is arranged an electronic control type EGR control valve
16. Further, around the EGR passage 15 is arranged a cooling device
17 for cooling the EGR gas flowing through the inside of the EGR
passage 15. In the embodiment shown in FIG. 1, the engine cooling
water is guided inside the cooling device 17 where the engine
cooling water is used to cool the EGR gas. On the other hand, each
fuel injector 3 is connected through a fuel feed pipe 18 to a
common rail 19. This common rail 19 is supplied inside it with fuel
from an electronic control type variable discharge fuel pump 20.
The fuel supplied to the inside of the common rail 19 is supplied
through the fuel feed pipes 18 to the fuel injectors 3.
[0034] An electronic control unit 30 is comprised of a digital
computer which is provided with components connected with each
other by a bi-directional bus 31 such as a ROM (read only memory)
32, RAM (random access memory) 33, CPU (microprocessor) 34, input
port 35, and output port 36. The SO.sub.x trap 11 has a temperature
sensor 21 attached to it so as to detect the temperature of the
SO.sub.x trap 11, while the NOx catalyst 12 has a temperature
sensor 22 attached to it so as to detect the temperature of the NOx
catalyst 12. The output signals of these temperature sensors 21 and
22 are input through the corresponding AD converters 37 to the
input port 35. Further, the NOx catalyst 12 has a pressure
difference sensor 23 attached to it for detecting the pressure
difference before and after the NOx catalyst 12. The output signal
of this pressure difference sensor 23 is input through the
corresponding AD converter 37 to the input port 35.
[0035] An accelerator pedal 40 is connected to a load sensor 41
generating an output voltage proportional to the depression amount
of the accelerator pedal 40. The output voltage of the load sensor
41 is input through the corresponding AD converter 37 to the input
port 35. Further, the input port 35 has a crank angle sensor 42
generating an output pulse every time the crankshaft rotates by for
example 15.degree. connected to it. On the other hand, the output
port 36 has the fuel injectors 3, throttle valve 9 drive step
motor, HC feed valve 14, EGR control valve 16, and fuel pump 20
connected to it through corresponding drive circuits 38.
[0036] Next, the NOx catalyst 12 will be explained. The NOx
catalyst 12 is carried on a monolithic carrier of a
three-dimensional mesh structure or a pellet-shaped carrier or is
carried on a particulate filter forming a honeycomb structure
(hereinafter referred to as "filter"). In this way, the NOx
catalyst 12 can be carried on various carriers, but below the case
of carrying the NOx catalyst 12 on a filter will be explained.
[0037] FIGS. 2(A) and (B) show the structure of the filter 12a
carrying the NOx catalyst 12. Note that FIG. 2(A) shows a front
view of the filter 12a, while FIG. 2(B) shows a side
cross-sectional view of the filter 12a. As shown in FIGS. 2(A) and
(B), the filter 12a forms a honeycomb structure and is provided
with a plurality of exhaust flow passages 60, 61 extending in
parallel with each other. These exhaust flow passages are comprised
of exhaust gas inflow passages 60 with downstream ends closed by
plugs 62 and exhaust gas outflow passages 61 with upstream ends
closed by plugs 63. Note that the hatched parts in FIG. 2(A) show
the plugs 63. Therefore, the exhaust gas inflow passages 60 and
exhaust gas outflow passages 61 are alternately arranged via thin
partition walls 64. In other words, the exhaust gas inflow passages
60 and exhaust gas outflow passages 61 are arranged so that each
exhaust gas inflow passage 60 is surrounded by four exhaust gas
outflow passages 61 and each exhaust gas outflow passage 61 is
surrounded by four exhaust gas inflow passages 60.
[0038] The filter 12a is for example formed from a porous material
such as cordierite. Therefore, the exhaust gas flowing into the
exhaust gas inflow passage 60, as shown by the arrows in FIG. 2(B),
passes through the surrounding partition walls 64 and flows out
into the adjoining exhaust gas outflow passages 61. When carrying
the NOx catalyst 12 on the filter 12a in this way, the peripheral
walls of the exhaust gas inflow passages 60 and exhaust gas outflow
passages 61, that is, the two side surfaces of the partition walls
64 and the inside walls of the fine holes in the partition walls
64, carry, for example, a catalyst carrier comprised of alumina.
FIG. 3 schematically shows a cross-section of the surface part of
this catalyst carrier 45. As shown in FIG. 3, on the surface of the
catalyst carrier 45, a precious metal catalyst 46 is carried
diffused in it. Further, on the surface of the catalyst carrier 45,
a layer of an NOx adsorbent 47 is formed.
[0039] Further, in the embodiment of the present invention, as the
precious metal catalyst 46, platinum (Pt) is used. As the
ingredient forming the NOx adsorbent 47, for example, at least one
ingredient selected from potassium (K), sodium (Na), cesium (Cs),
or another such alkali metal, barium (Ba), calcium (Ca), or another
such alkali earth, and lanthanum (La), yttrium (Y), or another such
rare earth is used.
[0040] If the ratio of the air and fuel (hydrocarbons) supplied
inside the engine intake passage, combustion chambers 2, and
exhaust passage upstream of the NOx catalyst 12 is referred to as
the "air-fuel ratio of the exhaust gas", the NOx adsorbent 47
absorbs the NOx when the air-fuel ratio of the exhaust gas is
leaner than even the stoichiometric air-fuel ratio and releases the
absorbed NOx when the oxygen concentration in the exhaust gas falls
in an "NO.sub.x absorption/release action".
[0041] That is, explaining the case of using barium (Ba) as the
ingredient forming the NOx adsorbent 47 as an example, when the
air-fuel ratio of the exhaust gas is lean, that is, when the oxygen
concentration in the exhaust gas is high, the NO contained in the
exhaust gas, as shown in FIG. 3, is oxidized on the platinum 46 and
becomes NO.sub.2, next this is absorbed in the NOx adsorbent 47
and, while bonding with the barium oxide (BaO), diffuses in the
form of nitric acid ions (NO.sub.3.sup.-) inside the NOx adsorbent
47. In this way, the NOx is absorbed inside the NOx adsorbent 47.
So long as the oxygen concentration in the exhaust gas is high,
NO.sub.2 is produced on the surface of the platinum 46. So long as
the NOx adsorption ability of the NOx adsorbent 47 is not
saturated, the NO.sub.2 is absorbed in the NOx adsorbent 47 and
nitric acid ions (NO.sub.3.sup.-) are produced.
[0042] As opposed to this, if supplying hydrocarbons from the HC
feed valve 14 so as to make the air-fuel ratio of the exhaust gas
the stoichiometric air-fuel ratio or richer than that, the oxygen
concentration in the exhaust gas falls, so the reaction proceeds in
the opposite direction (NO.sub.3.sup.-.fwdarw.NO.sub.2) and
therefore the nitric acid ions (NO.sub.3.sup.-) in the NOx
adsorbent 47 are released in the form of NO.sub.2 from the NOx
adsorbent 47. Next, the released NOx is reduced by the unburned HC
and CO contained in the exhaust gas.
[0043] In this way, when the air-fuel ratio of the exhaust gas is
lean, that is, when combustion is performed under a lean air-fuel
ratio, the NOx in the exhaust gas is absorbed in the NOx adsorbent
47. However, when combustion continues under a lean air-fuel ratio,
during that time the NOx adsorption ability of the NOx adsorbent 47
ends up becoming saturated and therefore the NOx adsorbent 47 ends
up no longer being able to absorb the NOx. Therefore, in the
embodiment according to the present invention, before the
adsorption ability of the NOx adsorbent 47 becomes saturated, HC is
supplied from the HC feed valve 14 so as to temporarily make the
air-fuel ratio of the exhaust gas rich and thereby make the NOx be
released from the NOx adsorbent 47.
[0044] However, exhaust gas contains SO.sub.x (sulfur oxides), that
is, SO.sub.2. If this SO.sub.2 flows into the NOx catalyst 12, this
SO.sub.2 is oxidized at the platinum 46 and becomes SO.sub.3. Next,
this SO.sub.3 is adsorbed in the NOx adsorbent 47 and, while
bonding with the barium oxide (BaO), diffuses in the NOx adsorbent
47 in the form of sulfuric acid ions (SO.sub.4.sup.2-) to produce
stable sulfate (BaSO.sub.4). However, the NOx adsorbent 47 has a
strong basicity, so this sulfate (BaSO.sub.4) is stable and hard to
break down. With just making the air-fuel ratio of the exhaust gas
rich, the sulfate (BaSO.sub.4) will not break down and will remain
as it is. Therefore, in the NOx adsorbent 47, as time elapses, the
sulfate (BaSO.sub.4) increases. Therefore, along with the elapse of
time, the NOx amount which can be absorbed by the NOx adsorbent 47
falls.
[0045] However, in this case, as explained at the start, if making
the air-fuel ratio of the exhaust gas flowing into the NOx catalyst
11 rich in the state of raising the temperature of the NOx catalyst
11 to the SO.sub.x release temperature of 600.degree. C. or more,
the NOx adsorbent 47 is made to release the SO.sub.x. However, in
this case, the NOx adsorbent 47 only releases a little SO.sub.x at
a time. Therefore, to make the NOx adsorbent 47 release all of the
absorbed SO.sub.x, the air-fuel ratio of the exhaust gas must be
made rich over a long time and therefore there is the problem that
a large amount of fuel or reducing agent becomes necessary.
Further, the SO.sub.x released from the SO.sub.x adsorbent 47 is
exhausted into the atmosphere. This is also not preferable.
[0046] Therefore, in the embodiment according to the present
invention, an SO.sub.x trap 11 is arranged upstream of the NOx
catalyst 12. This SO.sub.x trap 11 is used to trap the SO.sub.x
contained in the exhaust gas and thereby prevent SO.sub.x from
being sent into the NOx catalyst 12. Next, this SO.sub.x trap 11
will be explained.
[0047] This SO.sub.x trap 11 is comprised of for example a
honeycomb structure monolithic catalyst and has a large number of
exhaust gas circulation holes extending straight in the axial
direction of the SO.sub.x trap 11. When forming the SO.sub.x trap
11 from a honeycomb structure monolithic catalyst in this way, the
inner circumferential walls of the exhaust gas circulation holes
carry a catalyst carrier comprised of for example alumina. FIG. 4
schematically shows the cross-section of the surface part of the
catalyst carrier 50. As shown in FIG. 4, on the surface of the
catalyst carrier 50, a coat layer 51 is formed and carries the
precious metal catalyst 52 diffused on its surface.
[0048] In the embodiment according to the present invention, as the
precious metal catalyst 52, platinum (Pt) is used. As the
ingredient forming the coat layer 51, for example at least one
element selected from potassium (K), sodium (Na), cesium (Cs), or
another such alkali metal, barium (Ba), calcium (Ca), or another
such alkali earth, and lanthanum (La), yttrium (Y), or another such
rare earth is used. That is, the coat layer 51 of the SOx trap 11
exhibits a strong basicity.
[0049] Further, the SOx contained in the exhaust gas, mainly
SO.sub.2, as shown in FIG. 4, is oxidized on the platinum 52, then
is trapped in the coat layer 51. That is, the SO.sub.2 diffuses in
the coat layer 51 in the form of sulfuric acid ions
(SO.sub.4.sup.2-) and forms a sulfate. Note that in the
above-mentioned way, the coat layer 51 exhibits a strong basicity.
Therefore, as shown in FIG. 4, part of the SO.sub.2 contained in
the exhaust gas is directly trapped in the coat layer 51.
[0050] Further, exhaust gas also contains particulate matter. The
particulate matter contained in exhaust gas is trapped on the
filter 12a carrying the NOx catalyst 12 and successively oxidized.
However, if the amount of the trapped particulate matter becomes
greater than the amount of the particulate matter oxidized, the
particulate matter gradually deposits on the filter 12a. In this
case, if the amount of buildup of the particulate matter increases,
a drop in the engine output ends up being invited. Therefore, when
the amount of buildup of the particulate matter increases, the
builtup particulate matter must be removed. In this case, if
raising the temperature of the filter 12a to 600.degree. C. or so
under an excess of air, the builtup particulate matter is oxidized
and removed.
[0051] Thus, in an embodiment of the present invention, when the
amount of particulate matter built up on the filter 12a exceeds the
allowable amount, the temperature of the filter 12a is raised under
a lean air-fuel ratio of the exhaust gas and thereby the builtup
particulate matter is oxidized and removed. Specifically speaking,
in an embodiment of the present invention, when a pressure
difference before and after the filter 12a detected by a
differential pressure sensor 23 exceeds an allowable value, it is
judged that the amount of the builtup particulate matter has
exceeded the allowable amount. At this time, temperature elevation
control is performed for raising the temperature of the filter 12a
while keeping the air-fuel ratio of the exhaust gas flowing into
the filter 12a lean.
[0052] In this regard, the SOx trapping action of the
above-mentioned SOx trap 11 is performed when the air-fuel ratio of
the exhaust gas flowing into it is an air-fuel ratio leaner than
the stoichiometric air-fuel ratio and the temperature of the SOx
trap 11 is higher than a certain constant temperature (hereinafter
referred to as the "activation temperature"). On the other hand,
the SOx trap 11 ends up releasing the trapped SOx when the air-fuel
ratio of the exhaust gas flowing into it becomes the stoichiometric
air-fuel ratio or richer and its temperature becomes higher than a
certain constant temperature higher than the activation temperature
(hereinafter referred to as the "SOx release temperature").
Therefore, to prevent the SOx trap 11 from releasing SOx, it is
necessary to at least prevent the air-fuel ratio of the exhaust gas
flowing into the SOx trap 11 from becoming the stoichiometric
air-fuel ratio or richer and to prevent the temperature of the SOx
trap 11 from becoming higher than even the SOx release
temperature.
[0053] In this regard, even if the temperature of the SOx trap 11
as a whole becomes lower than the SOx release temperature,
sometimes the temperature will locally become higher than even the
SOx release temperature. At this time, the amount of SOx being
trapped in the SOx trap 11 (hereinafter referred to as "SOx trap
amount") becomes relatively large and exhaust gas of the
stoichiometric air-fuel ratio or a richer air-fuel ratio flows into
the SOx trap 11, so there is a possibility of part of the SOx trap
where the temperature locally becomes higher than the SOx release
temperature releasing SOx. Further, even if the air-fuel ratio of
the exhaust gas flowing into the SOx trap 11 becomes lean overall,
sometimes it locally becomes rich. At this time, if the SOx trap
amount of the SOx trap 11 becomes relatively large and the
temperature of the SOx trap 11 becomes higher than the SOx release
temperature, there is a possibility that part of the SOx trap 11
will release SOx. That is, to reliably prevent SOx from being
released from the SOx trap 11, when the SOx trap amount of the SOx
trap 11 becomes relatively large and the air-fuel ratio of the
exhaust gas flowing into the SOx trap 11 becomes the stoichiometric
air-fuel ratio or richer or when it is estimated it will become the
stoichiometric air-fuel ratio or richer, it is necessary to prevent
the temperature of the SOx trap 11 from becoming higher than the
SOx release temperature even locally. In the same way, to reliably
prevent the SOx trap 11 from releasing SOx, when the SOx trap
amount of the SOx trap 11 becomes relatively large and the
temperature of the SOx trap 11 becomes higher than the SOx release
temperature or is estimated as becoming higher, it is necessary to
prevent the air-fuel ratio of the exhaust gas flowing into the SOx
trap 11 from becoming the stoichiometric air-fuel ratio or richer
even locally.
[0054] Here, in the above-mentioned way, when trying to make the
NOx absorbent 47 release NOx, HC is fed from the HC feed valve 14
into the exhaust gas to make the air-fuel ratio of the exhaust gas
flowing into the NOx catalyst 12 the stoichiometric air-fuel ratio
or richer. Therefore, at this time, the air-fuel ratio of the
exhaust gas flowing into the SOx trap 11 also becomes the
stoichiometric air-fuel ratio or richer. Therefore, at this time,
if the SOx trap amount of the SOx trap 11 is relatively large, to
reliably prevent the SOx trap 11 from releasing SOx, it is
necessary to prevent the temperature of the SOx trap 11 from
becoming higher than the SOx release temperature even locally.
[0055] Thus, in an embodiment of the present invention, as the NOx
release control for making the NOx absorbent 47 release NOx, when
the SOx trap amount of the SOx trap 11 is smaller than a
predetermined amount (hereinafter referred to as "the predetermined
amount"), just NOx release control for making the NOx absorbent 47
release NOx (hereinafter referred to as "ordinary NOx release
control") is executed, while when the SOx trap amount of the SOx
trap 11 is larger than the predetermined amount, SOx release
suppression/NOx release control for keeping the SOx trap 11 from
releasing SOx while making the NOx absorbent 47 release NOx is
executed.
[0056] Next, ordinary NOx release control and SOx release
suppression/NOx release control employed as the NOx release control
of an exhaust purification system of the first embodiment will be
explained. Note that in the following description, the feed of HC
from the HC feed valve 14 into the exhaust gas will be referred to
as "HC feed", the amount of HC fed from the HC feed valve 14 into
the exhaust gas per unit time in each HC feed will be referred to
as the "HC feed rate", the time during which the HC is fed from the
HC feed valve 14 into the exhaust gas in one HC feed will be
referred to as the "HC feed time", the time interval at which each
HC feed is performed will be referred to as the "HC feed interval",
and the frequency by which HC feed is performed in one ordinary NOx
release control or SOx release suppression/NOx release control will
be referred to as the "HC feed frequency".
[0057] The ordinary NOx release control of the first embodiment is
performed when it is judged that the NOx absorbent 47 should
release NOx and when the SOx trap amount of the SOx trap 11 is
smaller than the predetermined amount. In this ordinary NOx release
control, as shown in FIG. 5(A), HC feed with an HC feed rate of a
predetermined HC feed rate (hereinafter referred to as an "ordinary
HC feed rate") Qa and with an HC feed time of a predetermined HC
feed time (hereinafter referred to as an "ordinary HC feed time")
Ta is performed at a predetermined HC feed interval (hereinafter
referred to as the "ordinary HC feed interval") Ia by a
predetermined HC feed frequency (hereinafter referred to as an
"ordinary HC feed frequency", in the example shown in FIG. 5(A),
three times).
[0058] Note that in the ordinary NOx release control in the first
embodiment, the HC feed rate in each HC feed, the HC feed time in
each HC feed, and the HC feed frequency are set so that the total
amount of HC fed to the NOx catalyst 12 when all of the HC feed
operations end becomes a sufficient HC amount for making the NOx
absorbent 47 release a predetermined amount of NOx (hereinafter
referred to as the "predetermined HC amount"). Therefore, according
to the ordinary NOx release control of the first embodiment, it is
possible to make the NOx absorbent 47 release a predetermined
amount of NOx.
[0059] On the other hand, the SOx release suppression/NOx release
control of the first embodiment is performed when it is judged that
the NOx absorbent 47 should release NOx and when the SOx trap
amount of the SOx trap 11 becomes greater than the predetermined
amount. In this SOx release suppression/NOx release control, as
shown in FIG. 5(B), HC feed with an HC feed rate of the HC feed
rate Qb smaller than the ordinary HC feed rate Qa and with an HC
feed time of a time Ta equal to the ordinary HC feed time Ta is
performed at an interval Ib shorter than the ordinary HC feed
interval Ia by a frequency larger than the ordinary HC feed
frequency. According to this, in one HC feed, the amount of HC fed
from the HC feed valve 14 into the exhaust gas is small, so the HC
fed from the HC feed valve 14 easily diffuses in the exhaust gas.
For this reason, formation of a region in the exhaust gas where the
air-fuel ratio locally very rich is suppressed, so the temperature
of the SOx trap 11 is kept from becoming higher than the locally
SOx release temperature. Therefore, the SOx trap 11 is reliably
kept from releasing SOx.
[0060] That is, if there is a region in the exhaust gas where the
air-fuel ratio locally becomes very rich, that is, a region in the
exhaust gas where locally HC is included in a very large amount,
the HC deposits to a partial region of the SOx trap 11 when the
exhaust gas flows into the SOx trap 11. If the deposited HC is
burned all at once in that partial region of the SOx trap 11, there
is a possibility that the temperature of that partial region will
become higher than the SOx release temperature. However, according
to the SOx release suppression/NOx release control of the first
embodiment, formation of a region in the exhaust gas where the
air-fuel ratio locally becomes very rich is suppressed, so the
temperature of the partial region of the SOx trap 11 is kept from
becoming higher than the SOx release temperature. Therefore, the
temperature of the SOx trap 11 is kept from locally becoming higher
than the SOx release temperature and the SOx trap 11 is reliably
kept from releasing SOx.
[0061] Note that in the SOx release suppression/NOx release control
of the first embodiment, as shown in FIG. 5(C), HC feed with an HC
feed rate of an HC feed rate Qb smaller than the ordinary HC feed
rate Qa and with an HC feed time of a time Tc longer than the
ordinary HC feed time may be performed at an interval Ic longer
than the ordinary HC feed interval Ia by the same frequency as the
ordinary HC feed frequency. According to this, the HC feed rate in
each HC feed operation is small, so the HC fed from the HC feed
valve 14 easily diffuses in the exhaust gas. For this reason, the
temperature of the SOx trap 11 is kept from locally becoming higher
than the SOx release temperature, so the SOx trap 11 is reliably
kept from releasing SOx.
[0062] Note that in the SOx release suppression/NOx release control
of the first embodiment, preferably the HC feed rate in each HC
feed, the HC feed time in each HC feed, and the HC feed frequency
are set so that the total amount of HC fed to the NOx catalyst 12
when all of the HC feed operations end becomes the predetermined HC
amount. Thus, in the example shown in FIG. 5(B), the HC feed rate
is made the HC feed rate Qb of half of the ordinary HC feed rate
Qa, the HC feed time is made the time Ta equal to the ordinary HC
feed time Ta, and the HC feed frequency is made a frequency double
the ordinary HC feed frequency. Note that in the example shown in
FIG. 5(B), the HC feed interval is made an interval Ib of half of
the ordinary HC feed interval Ia.
[0063] Further, in the example shown in FIG. 5(C), the HC feed rate
is made the HC feed rate Qb of half of the ordinary HC feed rate
Qa, the HC feed time is made the time Tc of double the ordinary HC
feed time Ta, and the HC feed frequency is made the same frequency
as the ordinary HC feed frequency.
[0064] Next, NOx release control of an exhaust purification system
of the second embodiment will be explained with reference to FIG.
6. Note that in FIGS. 6(A) to (C), the upper line shows the feed of
HC from the HC feed valve 14 into the exhaust gas, while the lower
line shows the injection of fuel from the fuel injector 3 in the
latter half of the expansion stroke or during an exhaust stroke of
a specific cylinder. Further, in the following explanation, the
injection of fuel from the fuel injector 2 in the latter half of
the expansion stroke or during the exhaust stroke of a specific
cylinder will be referred to as the "post fuel injection", the
amount of fuel injected from the fuel injector 2 per unit time in
each post fuel injection will be referred to as the "post fuel
injection rate", the time during which fuel is injected from the
fuel injector 2 in one post fuel injection will be referred to as
the "post fuel injection time", the time interval at which each
post fuel injection is performed will be referred to as the "post
fuel injection interval", and the frequency one post fuel injection
is performed will be referred to as the "post fuel injection
frequency".
[0065] In the NOx release control of the second embodiment, when it
is judged that the NOx absorbent 47 should release NOx (that is,
when the NOx release condition stands) and the SOx trap amount of
the SOx trap 11 is smaller than the predetermined amount (that is,
when the SOx release suppression condition does not stand),
ordinary NOx release control is executed. In this ordinary NOx
release control, as shown by the upper line of FIG. 6(A), an HC
feed with an HC feed rate of an HC feed rate Qa equal to the
ordinary HC feed rate Qa and with an HC feed time of a time Ta
equal to the ordinary HC feed time Ta is performed at intervals Ia
equal to the ordinary HC feed intervals Ia by the same frequency as
the ordinary frequency. Further, at this time, as shown by the
lower line of FIG. 6(A), none of the cylinders performs post fuel
injection. Of course, in the NOx release control of the second
embodiment as well, the HC feed rate in each HC feed, the HC feed
time in each HC feed, and the HC feed frequency are set so that the
total amount of HC fed to the NOx catalyst 12 when all of the HC
feed operations end becomes the predetermined HC amount.
[0066] On the other hand, in the NOx release control of the second
embodiment, when the NOx release condition stands and the SOx trap
amount of the SOx trap 11 is larger than the predetermined amount
(that is, when the SOx release suppression condition stands), SOx
release suppression/NOx release control is executed. In this SOx
release suppression/NOx release control, as shown by the upper line
of FIG. 6(B), HC feed with an HC feed rate of an HC feed rate Qb
smaller than the ordinary HC feed rate Qa and with an HC feed time
of a time Ta equal to the ordinary feed time is performed at an
interval Ia equal to the ordinary HC feed interval Ia by the same
frequency as the ordinary frequency and, as shown by the lower line
of FIG. 6(B), post fuel injection with a post fuel injection rate
of a post fuel injection rate Qbp smaller than the ordinary HC feed
rate Qa and with a post fuel injection time of a time Tap equal to
the ordinary HC feed time Ta is performed at an interval Iap equal
to the ordinary HC feed interval Ia by the same frequency as the
ordinary HC feed frequency. According to this, the amount of HC fed
from the HC feed valve 14 into the exhaust gas in one HC feed is
small, so the HC fed from the HC feed valve 14 easily diffuses in
the exhaust gas. For this reason, the HC injected from the HC feed
valve 14 is kept from causing the temperature of the SOx trap 11 to
locally become higher than the SOx release temperature.
Furthermore, the fuel injected from the fuel injector 3 at a
specific cylinder in the latter half of the expansion stroke or
during the exhaust stroke is modified by the heat in the cylinder
and lightened. The thus lightened fuel passes through the SOx trap
11 and is fed to the NOx catalyst 12, but this lightened fuel
easily diffuses in the exhaust gas. For this reason, the fuel
injected from the fuel injector 3 at a specific cylinder in the
latter half of the expansion stroke or during the exhaust stroke is
kept from causing the temperature of the SOx trap 11 from locally
becoming higher than the SOx release temperature. Therefore, the
SOx trap 11 is reliably kept from releasing SOx.
[0067] Note that in SOx release suppression/NOx release control of
the second embodiment, as shown in FIG. 6(C), it is also possible
to use just post fuel injection to feed HC (fuel) to the NOx
catalyst 12. That is, as shown by the lower line of FIG. 6(C), post
fuel injection with a post fuel injection rate of a post fuel
injection rate Qap equal to the ordinary HC feed rate Qa and with a
post fuel injection time of a time Tap equal to the ordinary HC
feed time Ta may be performed at an interval Iap equal to the
ordinary HC feed interval Ia by the same frequency as the ordinary
HC feed frequency. Of course, at this time, as shown by the upper
line of FIG. 6(C), HC is not fed from the HC feed valve 14 into the
exhaust gas. According to this, the fuel (HC) passing through the
SOx trap 11 and fed to the NOx catalyst 12 is lightened fuel, so
easily diffuses in the exhaust gas. For this reason, the
temperature of the SOx trap 11 is kept from locally becoming higher
than the SOx release temperature. Therefore, the SOx trap 11 is
reliably kept from releasing SOx.
[0068] Note that in SOx release suppression/NOx release control of
the second embodiment, the HC feed rate in each HC feed, the HC
feed time in each HC feed, and the HC feed frequency and the post
fuel injection rate at each post fuel injection, the post fuel
injection time at each post fuel injection, and the post fuel
injection frequency are preferably set so that the total amount of
HC (fuel) fed to the NOx catalyst 12 when all of the HC feed
operations and all of the post fuel injections end becomes the
predetermined HC (fuel) amount. Thus, in the example shown in FIG.
6(B), the HC feed rate is made an HC feed rate Qb of half of the
ordinary HC feed rate Qa, the HC feed time is made a time Ta equal
to the ordinary HC feed time Ta, the HC feed frequency is made a
frequency equal to the ordinary HC feed frequency, the post fuel
injection rate is made a post fuel injection rate Qbp of half of
the ordinary HC feed rate Qa, the post injection time is made a
time Tap equal to the ordinary HC feed time Ta, and the post fuel
injection frequency is made a frequency equal to the ordinary HC
feed frequency. Note that in the example shown in FIG. 6(B), the HC
feed interval and the post fuel injection interval are made
intervals Ia, Iap equal to the ordinary HC feed interval Ia.
[0069] Further, in the example shown in FIG. 6(C), the post fuel
injection rate is made a post fuel injection rate Qap equal to the
ordinary HC feed rate Qa, the post fuel injection time is made a
time Tap equal to the ordinary HC feed time Ta, and the post fuel
injection frequency is made a frequency equal to the ordinary HC
feed frequency. Note that in the example shown in FIG. 6(C), the
post fuel injection interval is made an interval Iap equal to the
ordinary HC feed interval Ia.
[0070] Note that in the example shown in FIG. 6, the post fuel
injection is shown executed at the same timing as the HC feed, but
the post fuel injection timing is controlled based on the crank
angle of the internal combustion engine, so strictly speaking, in
most cases, the post fuel injection timing will not become the same
timing as the HC feed timing, but will deviate from it somewhat.
Further, in the example shown in FIG. 6, the post fuel injection
interval was explained as equal to the ordinary HC feed interval,
but for the same reason, strictly speaking, in most cases, the post
fuel injection interval will not become equal to the ordinary HC
feed interval, but will deviate from it somewhat.
[0071] Note that when performing post fuel injection to feed fuel
to the NOx catalyst 12, the HC fed to the NOx catalyst when
performing the post fuel injection in the latter half of the
expansion stroke has a higher diffusion ability in the exhaust gas
compared with HC fed to the NOx catalyst 12 when performing the
post fuel injection during the exhaust stroke. Thus, in the
above-mentioned embodiment, as NOx release control, only post fuel
injection is employed as the method of feeding HC to the NOx
catalyst 12. In ordinary NOx release control, post fuel injection
is performed during the exhaust stroke to feed HC to the NOx
catalyst 12. On the other hand, in SOx release suppression/NOx
release control, it is also possible to feed HC to the NOx catalyst
12 by performing post fuel injection in the latter half of the
expansion stroke. This also enables the SOx trap 11 to be reliably
kept from releasing SOx.
[0072] Next, NOx release control of an exhaust purification system
of a third embodiment will be explained. In the NOx release control
of the third embodiment, when the NOx release condition stands and
the SOx release suppression condition does not stand, control the
same as the ordinary NOx release control of the first embodiment is
executed.
[0073] On the other hand, in NOx release control of the third
embodiment, when the NOx release condition stands and the SOx
release suppression condition stands, SOx release suppression/NOx
release control is executed. In this SOx release suppression/NOx
release control, in the same way as the ordinary NOx release
control of the above-mentioned first embodiment, the ordinary HC
feed rate, ordinary HC feed time, and, ordinary HC feed interval
are used for performing each HC feed by an ordinary HC feed
frequency, but HC lightened by fractional distillation is prepared
in advance and part of the HC fed from the HC feed valve 14 into
the exhaust gas in each HC feed is made this lightened HC. As
explained above, lightened HC easily diffuses in the exhaust gas.
For this reason, according to the SOx release suppression/NOx
release control of the third embodiment, the temperature of the SOx
trap 11 is kept from locally becoming higher than the SOx release
temperature. Therefore, the SOx trap 11 is reliably kept from
releasing SOx.
[0074] Next, NOx release control of an exhaust purification system
of a fourth embodiment will be explained. In the NOx release
control of the fourth embodiment, when the NOx release condition
stands and the SOx release suppression condition does not stand,
control the same as the ordinary NOx release control of the first
embodiment is executed.
[0075] On the other hand, in the NOx release control of the fourth
embodiment, when the NOx release condition stands and the SOx
release suppression condition stands, SOx release suppression/NOx
release control is executed. In this SOx release suppression/NOx
release control, the HC feed rate in each HC feed, the HC feed time
in each HC feed, and the HC feed interval are controlled so that
the temperature of the NOx catalyst 12 is kept lower than the
temperature of the NOx catalyst 12 corresponding to the temperature
of the SOx trap 11 at which the HC in the exhaust gas will end up
burning all at once in the SOx trap 11 (hereinafter referred to as
the "maximum NOx catalyst temperature"). That is, if the
temperature of the NOx catalyst 12 is higher than the maximum NOx
catalyst temperature, the temperature of the SOx trap 11 becomes
higher than the temperature at which the HC flowing into it ends up
being made to burn all at once. In this case, when the HC fed from
the HC feed valve 14 passes through the SOx trap 11, there is a
possibility that it will burn all at once, the temperature of the
SOx trap 11 will locally become higher than the SOx release
temperature, and the SOx trap 11 will release SOx. On the other
hand, according to SOx release suppression/NOx release control of
the fourth embodiment, the temperature of the NOx catalyst 12 is
kept lower than the maximum NOx catalyst temperature, so the HC
flowing into the SOx trap 11 is kept from burning all at once. For
this reason, the temperature of the SOx trap 11 is kept from
locally becoming higher than the SOx release temperature.
Therefore, the SOx trap 11 is reliably kept from releasing SOx.
[0076] Note that in the SOx release suppression/NOx release control
of the fourth embodiment, the HC feed rate in each HC feed, the HC
feed time in each HC feed, and the HC feed frequency are preferably
set so that the total amount of HC fed into the NOx catalyst 12
when all of the HC feed operations end becomes the predetermined
amount.
[0077] Next, NOx release control of an exhaust purification system
of a fifth embodiment will be explained. In the NOx release control
of the fifth embodiment, when the NOx release condition stands and
the SOx release suppression condition does not stand, control the
same as the ordinary NOx release control of the first embodiment is
executed.
[0078] On the other hand, in the NOx release control of the fifth
embodiment, when the NOx release condition stands and the SOx
release suppression condition stands, SOx release suppression/NOx
release control is executed. In this SOx release suppression/NOx
release control, the HC feed rate in each HC feed, the HC feed time
in each HC feed, and the HC feed interval are controlled so that
the amplitude of the rise and fall of the temperature of the NOx
catalyst 12 (hereinafter referred to as "temperature amplitude") is
kept smaller than the temperature amplitude of the NOx catalyst 12
allowed in ordinary NOx release control. That is, in SOx release
suppression/NOx release control, HC feed is intermittently
performed, so the NOx catalyst 12 is intermittently fed HC.
Further, when HC flows into the NOx catalyst 12, the heat of
reaction of the HC in the NOx catalyst 12 causes the temperature of
the NOx catalyst 12 to rise, then fall. Here, the temperature
amplitude of the NOx catalyst 12 being large means the amplitude of
the rise or fall of the temperature of the SOx trap 11 is also
large. Further, in this case, the temperature of the SOx trap 11
may at least locally become higher than the SOx release
temperature. Here, if the SOx trap amount of the SOx trap 11 is
greater than the predetermined amount, the SOx trap 11 may release
SOx. Thus, in the SOx release suppression/NOx release control of
the fifth embodiment, the HC feed rate in each HC feed, the HC feed
time in each HC feed, and the HC feed interval are controlled so
that the temperature amplitude of the NOx catalyst 12 is kept
smaller than the temperature amplitude of the NOx catalyst 12
allowed in ordinary NOx release control. According to this, the
temperature of the SOx trap 11 is kept from locally becoming higher
than the SOx release temperature. Therefore, the SOx trap 11 is
reliably kept from releasing SOx.
[0079] Note that in the SOx release suppression/NOx release control
of the fifth embodiment, the HC feed rate in each HC feed, the HC
feed time in each HC feed, and the HC feed frequency are preferably
set so that the total amount of HC fed into the NOx catalyst 12
when all of the HC feed operations end becomes the predetermined
amount.
[0080] Next, the NOx release control of the exhaust purification
system of a sixth embodiment will be explained. In the NOx release
control of the sixth embodiment, when the NOx release condition
stands and the SOx release suppression condition does not stand,
control the same as the ordinary NOx release control of the
above-mentioned first embodiment is executed.
[0081] On the other hand, in the NOx release control of the sixth
embodiment, when the NOx release condition stands and the SOx
release suppression condition stands, the SOx release
suppression/NOx release control is executed. In this SOx release
suppression/NOx release control, the HC feed rate in each HC feed,
the HC feed time in each HC feed, and the HC feed interval are
controlled so that the rich degree of the air-fuel ratio of the
exhaust gas fed into the NOx catalyst 12 is kept smaller than the
target rich degree in ordinary NOx release control. That is, when
the rich degree of the air-fuel ratio of the exhaust gas flowing
into the NOx catalyst 12 is large, the rich degree of the air-fuel
ratio of the exhaust gas flowing into the SOx trap 11 also becomes
large. Further, in this case, a region in the exhaust gas flowing
into the SOx trap 11 where the air-fuel ratio locally becomes very
rich may be formed. However, according to the SOx release
suppression/NOx release control of the sixth embodiment, formation
of a region in the exhaust gas flowing into the SOx trap 11 where
the air-fuel ratio locally becomes very rich is suppressed. For
this reason, the temperature of the SOx trap 11 is kept from
locally becoming higher than the SOx release temperature.
Therefore, the SOx trap 11 is reliably kept from releasing SOx.
[0082] Note that in the SOx release suppression/NOx release control
of the sixth embodiment, the rich degree of the air-fuel ratio of
the exhaust gas fed into the NOx catalyst 12 is for example
estimated from the output of an air-fuel ratio sensor provided in
the exhaust pipe downstream of the NOx catalyst 12.
[0083] Further, as explained above, the HC flowing into the SOx
trap 11 deposits at a partial region of the SOx trap 11. Here, if
the temperature of the region of the SOx trap 11 where the HC
deposits is low, the deposited HC will not burn but will remain
deposited there. Here, if the temperature of the region of the SOx
trap 11 where HC has deposited rises to the combustion temperature
of HC, the deposited HC may burn all at once. That is, the lower
the temperature of the SOx trap 11, the more possible it is that
the HC deposited on the SOx trap 11 will burn all at once. Thus, in
the SOx release suppression/NOx release control of the
above-mentioned sixth embodiment, when the rich degree of the
air-fuel ratio of the exhaust gas fed to the NOx catalyst 12 is
kept smaller than the target rich degree in ordinary NOx release
control, the lower the temperature of the SOx trap 11, the smaller
the rich degree of the air-fuel ratio of the exhaust gas fed to the
NOx catalyst 12 may be kept.
[0084] FIG. 7 shows an example of the routine for executing the NOx
release control of an embodiment of the present invention. In the
routine of FIG. 7, first, at step 10, it is judged if the NOx
amount .SIGMA.NOX absorbed in the NOx absorbent 47 is greater than
an allowable value .alpha. (.SIGMA.NOX>.alpha.) (that is,
whether the NOx release condition stands). Here, when it is judged
that .SIGMA.NOX.ltoreq..alpha., the routine is ended as is. On the
other hand, when it is judged that .SIGMA.NOX>.alpha., the
routine proceeds to step 11 where it is judged if the SOx trap
amount .SIGMA.SOX of the SOx trap 11 is greater than a
predetermined amount .beta. (.SIGMA.SOX>.beta.) (that is,
whether the SOx release suppression condition stands).
[0085] When it is judged at step 11 that .SIGMA.SOX>.beta., the
routine proceeds to step 12 where one of the SOx release
suppression/NOx release control of the above-mentioned first
embodiment to sixth embodiment is executed. On the other hand, when
it is judged at step 11 that .SIGMA.SOX.ltoreq..beta., the routine
proceeds to step 13 where one of the ordinary NOx release control
of the above-mentioned first embodiment to sixth embodiment is
executed.
[0086] In this regard, when, as explained above, the amount of
particulate matter built up on the filter 12a exceeds the allowable
value (that is, the PM removal condition stands), control is
executed for keeping the air-fuel ratio of the exhaust gas flowing
into the filter 12a lean while raising the temperature of the
filter 12a to a temperature of at least the temperature where the
particulate matter burns (hereinafter referred to as "PM combustion
temperature") to burn off the particulate matter deposited on the
filter 12a (hereinafter referred to as "PM removal control"). In
this PM removal control, to keep the air-fuel ratio of the exhaust
gas flowing into the filter 12a lean while raising the temperature
of the filter 12a, HC is fed from the HC feed valve 14 into the
exhaust gas in a range where the air-fuel ratio of the exhaust gas
flowing into the filter 12a is kept lean. That is, if the HC feed
valve 14 feeds HC into the exhaust gas, HC is fed to the filter
12a. At this time, if the air-fuel ratio of the exhaust gas flowing
into the filter 12a is kept lean, the HC burns on the filter 12a.
The heat of combustion generated at that time causes the
temperature of the filter 12a to rise. In this way, basically, when
PM removal control is executed, even if the HC feed valve 14 feeds
HC into the exhaust gas, the air-fuel ratio of the exhaust gas
flowing into the filter 12a is kept lean, so the air-fuel ratio of
the exhaust gas flowing into the SOx trap 11 is also kept lean.
Therefore, at this time, basically, the SOx trap 11 will not
release SOx.
[0087] In this regard, even if the air-fuel ratio of the exhaust
gas flowing into the SOx trap 11 was kept lean during the execution
of the PM removal control, if the SOx trap amount of the SOx trap
11 becomes relatively large, if there are regions in the exhaust
gas flowing into the SOx trap 11 where the air-fuel ratio is
locally rich and there are parts of the SOx trap 11 where the
temperature is locally higher than the SOx release temperature,
part of the SOx trap 11 may release SOx. Further, in PM removal
control, HC is fed from the HC feed valve 14 so as to raise the
temperature of the filter 12a to a temperature of at least the
relatively high temperature PM combustion temperature, but part of
the HC fed from the HC feed valve 14 burns at the SOx trap 11.
Therefore, during execution of PM removal control, the temperature
of the SOx trap 11 also becomes a relatively high temperature. For
this reason, during execution of PM removal control, the
temperature of the SOx trap 11 can be said to easily locally become
higher than the SOx release temperature. Whichever the case, to
reliably keep the SOx trap 11 from releasing SOx during execution
of PM removal control, when the SOx trap amount of the SOx trap 11
is relatively large, it is necessary to suppress the formation of a
region in the exhaust gas flowing into the SOx trap 11 where the
air-fuel ratio locally forms a rich region or to keep the
temperature of the SOx trap 11 from locally becoming higher than
the SOx release temperature.
[0088] Thus, in an embodiment of the present invention, as the PM
removal control for removing the particulate matter built up on the
filter 12a, when the SOx trap amount of the SOx trap 11 is smaller
than the predetermined amount, just PM removal control for burning
off the particulate matter built up on the filter 12a (hereinafter
referred to as "ordinary PM removal control") is executed. When the
SOx trap amount of the SOx trap 11 is larger than the predetermined
amount, PM removal control for keeping the SOx trap 11 from
releasing SOx while burning off the particulate matter built up on
the filter 12a (hereinafter referred to as "SOx release
suppression/PM removal control") is executed.
[0089] Next, the PM removal control of an exhaust purification
system of a seventh embodiment will be explained. In the PM removal
control of the seventh embodiment, when the amount of the
particulate matter built up on the filter 12a has exceeded an
allowable amount (that is, when the PM removal condition stands)
and the SOx trap amount of the SOx trap 11 is smaller than the
predetermined amount (that is, when the SOx release suppression
condition does not stand), ordinary PM removal control is executed.
In this ordinary PM removal control, as shown in FIG. 8(A), HC feed
with an HC feed rate of a predetermined HC feed rate (hereinafter
referred to as "ordinary HC feed rate") Qd and with an HC feed time
of a predetermined HC feed time (hereinafter referred to as
"ordinary HC feed time") Td is performed at a predetermined HC feed
interval (hereinafter referred to as "ordinary HC feed interval")
Id by a predetermined HC feed frequency (hereinafter referred to as
"ordinary HC feed frequency", in the example shown in FIG. 8(A),
three times).
[0090] Note that in the ordinary PM removal control of the seventh
embodiment, the HC feed rate in each HC feed, the HC feed time in
each HC feed, and the HC feed frequency are set so as to raise the
temperature of the filter 12a to the PM combustion temperature and
so that the total amount of HC fed to the filter 12a when all of
the HC feed operations end becomes an HC amount sufficient for
burning off exactly a predetermined amount of the particulate
matter built up on the filter 12a (hereinafter referred to as "the
predetermined HC amount"). Therefore, according to the ordinary PM
removal control of the seventh embodiment, it is possible to burn
off exactly a predetermined amount of the particulate matter built
up on the filter 12a.
[0091] On the other hand, in the PM removal control of the seventh
embodiment, when the PM removal condition stands and the SOx trap
amount of the SOx trap 11 is larger than the predetermined amount
(that is, when the SOx release suppression condition stands), SOx
release suppression/PM removal control is executed. In this SOx
release suppression/PM removal control, as shown in FIG. 8(B), HC
feed with a HC feed rate of an HC feed rate Qe smaller than the
ordinary HC feed rate Qd and with an HC feed time of a time Td
equal to the ordinary HC feed time Td is performed at an interval
Ie shorter than the ordinary HC feed interval Id by a frequency
greater than the ordinary HC feed frequency. According to this, the
amount of HC fed from the HC feed valve 14 into the exhaust gas in
one HC feed is small, so the HC fed from the HC feed valve 14
easily diffuses in the exhaust gas. For this reason, the formation
in the exhaust gas of a region where the air-fuel ratio becomes
locally rich is suppressed; so the release of SOx from the SOx trap
11 is reliably suppressed.
[0092] Note that in the SOx release suppression/NOx release control
of the seventh embodiment, as shown in FIG. 8(C), an HC feed with
an HC feed rate of an HC feed rate Qe smaller than the ordinary HC
feed rate Qd and with an HC feed time of a time Tf longer than the
ordinary HC feed time may also be performed at an interval If
longer than the ordinary HC feed interval Id by the same frequency
as the ordinary HC feed frequency. According to this, the HC feed
rate in each HC feed is small, so the HC fed from the HC feed valve
14 easily diffuses in the exhaust gas. For this reason, the
formation in the exhaust gas of a region where the air-fuel ratio
becomes locally rich is suppressed, so the release of SOx from the
SOx trap 11 is reliably suppressed.
[0093] Note that in the SOx release suppression/PM removal control
of the seventh embodiment, the HC feed rate in each HC feed, the HC
feed time in each HC feed, the HC feed interval, and the HC feed
frequency are set to at least enable the temperature of the filter
12a to be raised to the PM combustion temperature.
[0094] Further, in the SOx release suppression/PM removal control
of the seventh embodiment as well, the HC feed rate in each HC
feed, the HC feed time in each HC feed, and the HC feed frequency
are preferably set so that the total amount of HC fed to the filter
12a when all of the HC feed operations end becomes the
predetermined amount. Thus, in the example shown in FIG. 8(B), the
HC feed rate is made the HC feed rate Qe of half of the ordinary HC
feed rate Qd, the HC feed time is made a time Td equal to the
ordinary HC feed time Td, and the HC feed frequency is made a
frequency twice the ordinary HC feed frequency. Note that in the
example shown in FIG. 8(Bs), the HC feed interval is made an
interval Ie of half of the ordinary HC feed intervals Id.
[0095] Further, in the example shown in FIG. 8(C), the HC feed rate
is made an HC feed rate Qe of half of the ordinary HC feed rate Qd,
the HC feed time is made a time Tf of double the ordinary HC feed
time Td, and the HC feed frequency is made a frequency equal to the
ordinary HC feed frequency so that the total amount of HC fed to
the filter 12a when all of the HC feed operations end becomes the
predetermined amount. Note that in the example shown in FIG. 8(C),
the HC feed interval is made an interval of about 1.5 times the
ordinary HC feed interval.
[0096] Next, the PM removal control of the exhaust purification
system of an eighth embodiment will be explained with reference to
FIG. 9. Note that in FIGS. 9(A) to (C), the upper line shows the
feed of HC from the HC feed valve 14 into the exhaust gas, while
the lower line shows the injection of fuel from the fuel injector 3
at a specific cylinder in the latter half of the expansion stroke
or during the exhaust stroke.
[0097] In the PM removal control of the eighth embodiment, when the
PM removal condition stands and the SOx release suppression
condition does not stand, ordinary PM removal control is executed.
In this ordinary PM removal control, as shown by the upper line of
FIG. 9(A), an HC feed with a HC feed rate of an HC feed rate Qd
equal to the ordinary HC feed rate Qd and with an HC feed time of a
time Td equal to the ordinary HC feed time Td is performed at an
interval Id equal to the ordinary HC feed interval Id by the same
frequency as the ordinary frequency. Further, at this time, as
shown by the lower line of FIG. 9(A), no cylinder is performing
post fuel injection. Of course, in the ordinary PM removal control
of the eighth embodiment as well, the HC feed rate in each HC feed,
the HC feed time in each HC feed, and the HC feed frequency are set
so as to raise the temperature of the filter 12a to the PM
combustion temperature and so that the total amount of HC fed to
the filter 12a when all of the HC feed operations end becomes the
predetermined amount.
[0098] On the other hand, in the PM removal control of the eighth
embodiment, when the PM removal condition stands and the SOx
release suppression condition stands, SOx release suppression/PM
removal control is executed. In this SOx release suppression/PM
removal control, as shown by the upper line of FIG. 9(B), an HC
feed with an HC feed rate of an HC feed rate Qe smaller than the
ordinary HC feed rate Qd and with an HC feed time of a time Td
equal to the ordinary feed time is performed at an interval Id
equal to the ordinary HC feed interval Id by a frequency the same
as the ordinary frequency and, as shown by the lower line of FIG.
9(B), post fuel injection with a post fuel injection rate of a post
fuel injection rate Qep smaller than the ordinary HC feed rate Qd
and with a post fuel injection time of a time Tdp equal to the
ordinary HC feed time Td is performed at an interval Idp equal to
the ordinary HC feed interval Id by a frequency the same as the
ordinary HC feed frequency. According to this, the amount of HC fed
into the exhaust gas from the HC feed valve 14 in one HC feed is
small, so the HC fed from the HC feed valve 14 easily diffuses in
the exhaust gas. For this reason, the HC fed from the HC feed valve
14 is kept from causing the formation of a region in the exhaust
gas where the air-fuel ratio locally becomes very rich.
Furthermore, the fuel injected from the fuel injector 3 at a
specific cylinder in the latter half of the expansion stroke or
during the exhaust stroke is modified by the heat in the cylinder
and lightened. Further, this lightened fuel easily diffuses in the
exhaust gas. For this reason, the fuel injected from the fuel
injector 3 at a specific cylinder in the latter half of the
expansion stroke or during the exhaust stroke is kept from causing
the formation of a region in the exhaust gas where the air-fuel
ratio locally becomes very rich. Therefore, the SOx trap 11 is
reliably kept from releasing SOx.
[0099] Note that in the SOx release suppression/PM removal control
of the eighth embodiment, as shown in FIG. 9(C), it is also
possible to use just the post fuel injection to feed HC (fuel) into
the filter 12a. That is, as shown by the lower line of FIG. 9(C),
post fuel injection with a post fuel injection rate of a post fuel
injection rate Qdp equal to the ordinary HC feed rate Qd and with a
post fuel injection time of a time Tdp equal to the ordinary HC
feed time Td may be performed at an interval Idp equal to the
ordinary HC feed interval Id by a frequency equal to the ordinary
HC feed frequency. Of course, at this time, as shown by the upper
line of FIG. 9(C), the HC feed valve 14 does not feed HC into the
exhaust gas. According to this, the fuel (HC) passing through the
SOx trap 11 and fed to the filter 12a is lightened fuel, so easily
diffuses in the exhaust gas. For this reason, formation of a region
in the exhaust gas where the air-fuel ratio locally becomes very
rich is suppressed, so the SOx trap 11 is reliably kept from
releasing SOx.
[0100] Note that in the SOx release suppression/NOx release control
of the eighth embodiment, the HC feed rate in each HC feed, the HC
feed time in each HC feed, the HC feed interval, and the HC feed
frequency are set so as to at least enable the temperature of the
filter 12a to be raised to the PM combustion temperature.
[0101] Further, in the SOx release suppression/PM removal control
of the eighth embodiment as well, the HC feed rate in each HC feed,
the HC feed time in each HC feed, and the HC feed frequency and the
post fuel injection rate in each post fuel injection, the post fuel
injection time in each post fuel injection, and the post fuel
injection frequency are preferably set so that the total amount of
HC (fuel) fed to the filter 12a when all of the HC feed operations
and all of the post fuel injections end becomes the predetermined
HC (fuel). Thus, in the example shown in FIG. 9(B), the HC feed
rate is made an HC feed rate Qe of half of the ordinary HC feed
rate Qd, the HC feed time is made a time Td equal to the ordinary
HC feed time Td, the HC feed frequency is made a frequency equal to
the ordinary HC feed frequency, the post fuel injection rate is
made a post fuel injection rate Qdp of half of the ordinary HC feed
rate Qd, the post injection time is made a time Tdp equal to the
ordinary HC feed time Td, and the post fuel injection frequency is
made a frequency equal to the ordinary HC feed frequency. Note that
in the example shown in FIG. 9(B), the HC feed interval and the
post fuel injection intervals are both made intervals Id, Idp equal
to the ordinary HC feed interval Id.
[0102] Further, in the example shown in FIG. 9(C), the post fuel
injection rate is made a post fuel injection rate Tdp equal to the
ordinary HC feed rate Qd, the post fuel injection time is made a
time Tdp equal to the ordinary HC feed time Td, and the post fuel
injection frequency is made a frequency equal to the ordinary HC
feed frequency so that the total amount of HC (fuel) fed to the
filter 12a when all of the HC feed operations and all of the post
fuel injections end becomes the predetermined HC (fuel). Note that
in the example shown in FIG. 9(C), the post fuel injection interval
is made an interval Tdp equal to the ordinary HC feed interval
Id.
[0103] Note that in the example shown in FIG. 9, the post fuel
injection is shown executed at the same timing as the HC feed, but
the post fuel injection timing is controlled based on the crank
angle of the internal combustion engine, so strictly speaking, in
most cases, the post fuel injection timing will not become the same
timing as the HC feed timing, but will deviate from it somewhat.
Further, in the example shown in FIG. 9, the post fuel injection
interval was explained as equal to the ordinary HC feed interval,
but for the same reason, strictly speaking, in most cases, the post
fuel injection interval will not become equal to the ordinary HC
feed interval, but will deviate from it somewhat.
[0104] Next, PM removal control of an exhaust purification system
of a ninth embodiment will be explained. In the PM removal control
of the ninth embodiment, when the PM removal condition stands and
the SOx release suppression condition does not stand, the same
control as the ordinary PM removal control of the seventh
embodiment is executed.
[0105] On the other hand, in the PM removal control of the ninth
embodiment, when the PM removal condition stands and the SOx
release suppression condition stands, SOx release suppression/PM
removal control is executed. In this SOx release suppression/PM
removal control, in the same way as the ordinary NOx release
control of the seventh embodiment, the ordinary HC feed rate,
ordinary HC feed time, and ordinary HC feed interval are used for
performing each HC feed by the ordinary HC feed frequency, but HC
lightened by fractional distillation is prepared in advance and, in
each HC feed, part of the HC fed from the HC feed valve 14 into the
exhaust gas is made this lightened HC. In the above-mentioned way,
the lightened HC easily diffuses in the exhaust gas. For this
reason, the formation in the exhaust gas of a region where the
air-fuel ratio becomes locally rich is suppressed, so the release
of SOx from the SOx trap 11 is reliably suppressed.
[0106] Next, the PM removal control of the exhaust purification
system of the 10th embodiment will be explained. In the PM removal
control of the 10th embodiment, when the PM removal condition
stands and the SOx release suppression condition does not stand,
the same control as in the ordinary PM removal control of the
seventh embodiment is executed.
[0107] On the other hand, in the PM removal control of the 10th
embodiment, when the PM removal condition stands and the SOx
release suppression condition stands, the SOx release
suppression/PM removal control is executed. In this SOx release
suppression/PM removal control, the HC feed rate in each HC feed,
the HC feed time in each HC feed, and the HC feed interval are
controlled so that the temperature of the SOx trap 11 is kept lower
than the temperature where the HC in the exhaust gas ends up being
burned all at once at the SOx trap 11. According to this, even when
a region where the air-fuel ratio becomes locally rich is formed in
the exhaust gas, the HC is kept from burning all at once at the SOx
trap 11. For this reason, the temperature of the SOx trap 11 is
kept from locally becoming higher than the SOx release temperature,
so the SOx trap 11 is reliably kept from releasing SOx.
[0108] Note that in the SOx release suppression/PM removal control
of the 10th embodiment, the HC feed rate in each HC feed, the HC
feed time in each HC feed, the HC feed interval, and the HC feed
frequency are set so as to at least enable the temperature of the
filter 12a to be raised to the PM combustion temperature.
[0109] Further, in the SOx release suppression/PM removal control
of the 10th embodiment as well, the HC feed rate in each HC feed,
the HC feed time in each HC feed, and the HC feed frequency are
preferably set so that the total amount of HC fed to the filter 12a
becomes the predetermined amount when all of the HC feed operations
end.
[0110] Next, the PM removal control of an exhaust purification
system of the 11th embodiment will be explained. In the PM removal
control of the 11th embodiment, when the PM removal condition
stands and the SOx release suppression condition does not stand,
control the same as the ordinary PM removal control of the seventh
embodiment is executed.
[0111] On the other hand, in the PM removal control of the 11th
embodiment, when the PM removal condition stands and the SOx
release suppression condition stands, SOx release suppression/PM
removal control is executed. In this SOx release suppression/PM
removal control, the HC feed rate in each HC feed, the HC feed time
in each HC feed, and the HC feed interval are controlled so that
the temperature of the filter 12a is kept at a temperature as close
as possible to the PM combustion temperature. According to this,
the HC feed rate at one HC feed is set small, the HC feed time in
one HC feed is set short, or the HC feed interval is set long.
Therefore, the HC fed from the HC feed valve 14 easily diffuses in
the exhaust gas. For this reason, the formation in the exhaust gas
of a region where the air-fuel ratio becomes locally rich is
suppressed, so the release of SOx from the SOx trap 11 is reliably
suppressed.
[0112] Note that in the SOx release suppression/PM removal control
of the 11th embodiment, the HC feed rate in each HC feed, the HC
feed time in each HC feed, the HC feed interval, and the HC feed
frequency are set so as to at least enable the temperature of the
filter 12a to be raised to the PM combustion temperature.
[0113] Further, in the SOx release suppression/PM removal control
of the 11th embodiment as well, the HC feed rate in each HC feed,
the HC feed time in each HC feed, and the HC feed frequency are
preferably set so that the total amount of HC fed to the filter 12a
becomes the predetermined amount when all of the HC feed operations
end. In this case, the time during which the SOx release
suppression/PM removal control is executed becomes longer than the
time during which ordinary PM removal control is executed.
[0114] Next, PM removal control of an exhaust purification system
of a 12th embodiment will be explained. In the PM removal control
of the 12th embodiment, when the PM removal condition stands and
the SOx release suppression condition does not stand, the same
control as the ordinary PM removal control of the seventh
embodiment is executed.
[0115] On the other hand, in the PM removal control of the 12th
embodiment, when the PM removal condition stands and the SOx
release suppression condition stands, SOx release suppression/PM
removal control is executed. In this SOx release suppression/PM
removal control, the HC feed rate in each HC feed, the HC feed time
in each HC feed, and the HC feed interval are controlled so that
the width of the rise or fall of the temperature of the SOx trap 11
(hereinafter referred to as the "temperature amplitude") is kept
smaller than the temperature amplitude of the SOx trap 11 allowed
in ordinary PM removal control. According to this, compared with
during execution of ordinary PM removal control, the HC feed rate
in each HC feed is set smaller, the HC feed time in each HC feed is
set shorter, or the HC feed interval is set longer. For this
reason, the HC fed from the HC feed valve 14 easily diffuses in the
exhaust gas. Therefore, the formation in the exhaust gas of a
region where the air-fuel ratio becomes locally rich is suppressed,
so the release of SOx from the SOx trap 11 is reliably
suppressed.
[0116] Note that in the SOx release suppression/PM removal control
of the 12th embodiment, the HC feed rate in each HC feed, the HC
feed time in each HC feed, and the HC feed frequency are set to
enable at least the temperature of the filter 12a to be raised to
the PM combustion temperature.
[0117] Further, in the SOx release suppression/PM removal control
of the 12th embodiment as well, the HC feed rate in each HC feed,
the HC feed time in each HC feed, and the HC feed frequency are
preferably set so that the total amount of HC fed to the filter 12a
when all of the HC feeds end becomes a predetermined HC amount.
[0118] Next, the PM removal control of the exhaust purification
system of the 13th embodiment will be explained. In the PM removal
control of the 13th embodiment, when the PM removal condition
stands and the SOx release suppression condition does not stand,
the same control as the ordinary PM removal control of the seventh
embodiment is executed.
[0119] On the other hand, in the PM removal control of the 13th
embodiment, when the PM removal condition stands and the SOx
release suppression condition stands, the SOx release
suppression/PM removal control is executed. In this SOx release
suppression/PM removal control, the HC feed rate in each HC feed,
the HC feed time in each HC feed, and the HC feed interval are
controlled so that the lean degree of the air-fuel ratio of the
exhaust gas fed to the filter 12a is kept larger than the target
lean degree in the ordinary PM removal control. That is, when the
lean degree of the air-fuel ratio of the exhaust gas flowing into
the filter 12a is small, the lean degree of air-fuel ratio of the
exhaust gas flowing into the SOx trap 11 also becomes small.
Further, in this case, a region in the exhaust gas flowing into the
SOx trap 11 where the air-fuel ratio locally becomes rich may be
formed. However, according to the SOx release suppression/PM
removal control of the 13th embodiment, the formation of a region
in the exhaust gas flowing into the SOx trap 11 where the air-fuel
ratio becomes locally rich is suppressed, so the release of SOx
from the SOx trap 11 is reliably suppressed.
[0120] Note that in the SOx release suppression/PM removal control
of the 13th embodiment, the HC feed rate in each HC feed, the HC
feed time in each HC feed, and the HC feed frequency are set to
enable at least the temperature of the filter 12a to be raised to
the PM combustion temperature.
[0121] Further, in the SOx release suppression/PM removal control
of the 13th embodiment as well, the HC feed rate in each HC feed,
the HC feed time in each HC feed, and the HC feed frequency are
preferably set so that the total amount of HC fed to the filter 12a
when all of the HC feeds end becomes a predetermined HC amount.
[0122] Further, in the SOx release suppression/PM removal control
of the 13th embodiment, the lean degree of the air-fuel ratio of
the exhaust gas fed to the filter 12a is, for example, estimated
from the output of the air-fuel ratio sensor attached to exhaust
pipe downstream of the filter 12a.
[0123] Next, the PM removal control of an exhaust purification
system of the 14th embodiment will be explained. In the PM removal
control of the 14th embodiment, when the PM removal condition
stands and the SOx release suppression condition does not stand,
control the same as the ordinary PM removal control of the seventh
embodiment is executed.
[0124] On the other hand, in the PM removal control of the 14th
embodiment, when the PM removal condition stands and the SOx
release suppression condition stands, SOx release suppression/PM
removal control is executed. In this SOx release suppression/PM
removal control, the HC feed rate in each HC feed, the HC feed time
in each HC feed, and the HC feed interval are controlled so that
the temperature elevation rate when the filter 12a is raised in
temperature is kept smaller than the target temperature elevation
rate in ordinary PM removal control. According to this, the HC feed
rate in one HC feed is set smaller, the HC feed time in one HC feed
is set shorter, or the HC feed interval is set longer. For this
reason, the HC fed from the HC feed valve 14 easily diffuses in the
exhaust gas. For this reason, the formation in the exhaust gas of a
region where the air-fuel ratio becomes locally rich is suppressed,
so the release of SOx from the SOx trap 11 is reliably
suppressed.
[0125] Note that in the SOx release suppression/PM removal control
of the 14th embodiment, the HC feed rate in each HC feed, the HC
feed time in each HC feed, the HC feed interval, and the HC feed
frequency are set so as to at least enable the temperature of the
filter 12a to be raised to the PM combustion temperature.
[0126] Further, in the SOx release suppression/PM removal control
of the 14th embodiment as well, the HC feed rate in each HC feed,
the HC feed time in each HC feed, and the HC feed frequency are
preferably set so that the total amount of HC fed to the filter 12a
when all of the HC feed operations end becomes the predetermined
amount.
[0127] FIG. 10 shows an example of a routine for executing the PM
removal control of an embodiment of the present invention. In the
routine of FIG. 10, first, at step 20, it is judged if the amount
.SIGMA.PM of particulate matter deposited on the filter 12a is
greater than an allowable value .gamma. (.SIGMA.PM>.gamma.)
(that is, if the PM removal condition stands). Here, when it is
judged that .SIGMA.PM.ltoreq..gamma., the routine is ended as is.
On the other hand, when it is judged that .SIGMA.PM>.gamma., the
routine proceeds to step 21 where it is judged if the SOx trap
amount .SIGMA.SOX of the SOx trap 11 is greater than a
predetermined amount .beta. (.SIGMA.SOX>.beta.) (that is,
whether the SOx release suppression condition stands).
[0128] When it is judged at step 21 that .SIGMA.SOX>.beta., the
routine proceeds to step 22 where the SOx release suppression/PM
removal control of one of the above-mentioned seventh embodiment to
the 14th embodiment is executed. On the other hand, when it is
judged at step 21 that .SIGMA.SOX.ltoreq..beta., the routine
proceeds to step 23 where the SOx release suppression/PM removal
control of one of the above-mentioned seventh embodiment to the
14th embodiment is executed.
[0129] However, when trying to make the NOx absorbent 47 release
NOx and the temperature of the SOx trap 11 becomes higher than the
SOx release temperature, if feeding HC from the HC feed valve 14
into the exhaust gas so as to make the NOx absorbent 47 release
NOx, the SOx trap 11 ends up releasing SOx. Thus, as NOx release
control of an exhaust purification system of the 15th embodiment,
when trying to make the NOx absorbent 47 release NOx (that is, when
the NOx release condition stands), it is possible to prohibit the
feed of HC from the HC feed valve 14 into the exhaust gas (that is,
the execution of NOx release control in the above-mentioned
embodiment) if the temperature of the SOx trap 11 becomes higher
than the SOx release temperature. According to this, the SOx trap
11 is reliably kept from releasing SOx.
[0130] FIG. 11 shows an example of a routine executing NOx release
control of a 15th embodiment. In the routine of FIG. 11, first, at
step 30, it is judged if the NOx amount .SIGMA.NOX absorbed in the
NOx absorbent 47 is greater than an allowable value .alpha.
(.SIGMA.NOX>.alpha.) (that is, whether the NOx release condition
stands). Here, when it is judged that .SIGMA.NOX.ltoreq..alpha.,
the routine is ended as is. On the other hand, when it is judged
that .SIGMA.NOX>.alpha., the routine proceeds to step 31 where
it is judged if the temperature Tsox of the SOx trap 11 is the SOx
release temperature Tth or more (Tsox.gtoreq.Tth).
[0131] When it is judged at step 31 that Tsox.gtoreq.Tth, the
routine proceeds to step 32 where execution of NOx release control
is prohibited. That is, in this case, the NOx release control is
not executed. On the other hand, when it is judged at step 31 that
Tsox<Tth, the routine proceeds to step 33, where it is judged if
the SOx trap amount ESOX of the SOx trap 11 is greater than a
predetermined amount .beta. (.SIGMA.SOX>.beta.) (that is,
whether the SOx release suppression condition stands).
[0132] When it is judged at step 33 that .SIGMA.SOX>.beta., the
routine proceeds to step 34, where SOx release suppression/NOx
release control of one of the above-mentioned first embodiment to
sixth embodiment is executed. On the other hand, when it is judged
at step 33 that .SIGMA.SOX.ltoreq..beta., the routine proceeds to
step 35 where one of the ordinary NOx release control of the
above-mentioned first embodiment to sixth embodiment is
executed.
[0133] However, as the PM removal control of the exhaust
purification system of the 16th embodiment, the following control
may also be employed. That is, as explained above, during execution
of PM removal control, the temperature of the SOx trap 11 becomes
relatively high, but here when the temperature of the SOx trap 11
is higher than the SOx release temperature, compared with when the
temperature of the SOx trap 11 is lower than the SOx release
temperature, the formation in the exhaust gas of a region where the
air-fuel ratio locally becomes rich should be reliably suppressed.
Thus, in the PM removal control of the 16th embodiment, when the PM
removal condition stands and the SOx release suppression condition
does not stand, one of the SOx release suppression/PM removal
control of the above-mentioned seventh embodiment to 14th
embodiment is executed.
[0134] On the other hand, in the PM removal control of the 16th
embodiment, when the PM removal condition stands and the SOx
release suppression condition stands, it is judged that the
temperature of the SOx trap 11 is higher than the SOx release
temperature. Here, when the temperature of the SOx trap 11 is lower
than the SOx release temperature, either of the SOx release
suppression/PM removal control of the above-mentioned seventh
embodiment to the 14th embodiment is executed. On the other hand,
when the temperature of the SOx trap 11 is higher than the SOx
release temperature, similar control as the SOx release
suppression/PM removal control performed when the temperature of
the SOx trap 11 is lower than the SOx release temperature is
executed, but the HC feed rate at this time is made smaller than
the HC feed rate in the SOx release suppression/PM removal control
performed when the temperature of the SOx trap 11 is lower than the
SOx release temperature. According to this, the amount of HC fed
from the HC feed valve 14 in one HC feed is small, so the HC fed
from the HC feed valve 14 easily diffuses in the exhaust gas. For
this reason, the formation in the exhaust gas of a region where the
air-fuel ratio becomes locally rich is suppressed, so the release
of SOx from the SOx trap 11 is suppressed.
[0135] Alternatively, in the above-mentioned PM removal control of
the 16th embodiment, when the PM removal condition stands and the
SOx release suppression condition stands, the HC feed rate in each
HC feed, the HC feed time in each HC feed, and the HC feed interval
may be controlled so that the width of the rise or fall of the
temperature of the SOx trap 11 (temperature amplitude) when the
temperature of the SOx trap 11 is higher than the SOx release
temperature is kept smaller than the temperature amplitude of the
SOx trap 11 allowed in the SOx release/PM removal control performed
when the temperature of the SOx trap 11 is lower than the SOx
release temperature. According to this, compared with execution of
the SOx release suppression/PM removal control performed when the
temperature of the SOx trap 11 is lower than the SOx release
temperature, the HC feed rate in each HC feed is set smaller, the
HC feed time in each HC feed is set shorter, or the HC feed
interval is set longer. For this reason, the HC fed from the HC
feed valve 14 easily diffuses in the exhaust gas. Therefore, the
formation in the exhaust gas of a region where the air-fuel ratio
becomes locally rich is suppressed, so the release of SOx from the
SOx trap 11 is reliably suppressed.
[0136] FIG. 12 shows an example of the routine executing the PM
removal control of the 16th embodiment. In the routine of FIG. 12,
first, at step 40, it is judged if the amount .SIGMA.PM of the
particulate matter deposited on the filter 12a is greater than an
allowable value .gamma. (.SIGMA.PM>.gamma.) (that is, whether
the PM removal condition stands). Here, when it is judged that
.SIGMA.PM.ltoreq..gamma., the routine is ended as is. On the other
hand, when it is judged that .SIGMA.PM>.gamma., the routine
proceeds to step 41 where it is judged if the SOx trap amount
.SIGMA.SOX of the SOx trap 11 is greater than a predetermined
amount .gamma. (.SIGMA.SOX>.beta.) (that is, whether the SOx
release suppression condition stands).
[0137] When it is judged at step 41 that .SIGMA.SOX.ltoreq..beta.,
the routine proceeds to step 45 where one of the ordinary PM
removal control of the seventh embodiment to 14th embodiment is
executed. On the other hand, when it is judged at step 41 that
.SIGMA.SOX>.beta., the routine proceeds to step 42 where it is
judged if the temperature Tsox of the SOx trap 11 is the SOx
release temperature Tth or more (Tsox.gtoreq.Tth).
[0138] When it is judged at step 42 that Tsox<Tth, the routine
proceeds to step 44 where SOx release suppression/PM removal
control II is executed. In this SOx release suppression/PM removal
control II, one of the SOx release suppression/PM removal control
of the seventh embodiment to the 14th embodiment is executed. On
the other hand, when it is judged at step 42 that Tsox.gtoreq.Tth,
the routine proceeds to step 45 where SOx release suppression/PM
removal control I is executed. In this SOx release suppression/PM
removal control I, control similar to the SOx release
suppression/PM removal control II of step 44 is executed, but here
the HC feed rate is made smaller than the HC feed rate at the SOx
release suppression/PM removal control II of step 44.
[0139] In this regard, it is also possible to employ the following
control as NOx release control of an exhaust purification system of
a 17th embodiment. That is, in the NOx release control of the 17th
embodiment, when the lean degree of the air-fuel ratio of the
exhaust gas exhausted from each cylinder is larger than a
predetermined lean degree (hereinafter referred to as "the
predetermined lean degree"), one of the ordinary NOx release
control of the first embodiment to sixth embodiment is executed
when the NOx release condition stands. On the other hand, when the
lean degree of the air-fuel ratio of the exhaust gas exhausted from
each cylinder is smaller than the predetermined lean degree, one of
the SOx release suppression/NOx release control of the first
embodiment to sixth embodiment is executed when the NOx release
condition stands. According to this, the SOx trap 11 is reliably
kept from releasing SOx.
[0140] That is, when the lean degree of the air-fuel ratio of the
exhaust gas exhausted from each cylinder is smaller than the
predetermined lean degree, the air-fuel ratio of the exhaust gas
becomes close to a rich air-fuel ratio. At this time, if NOx
release control is executed, there is a high possibility that a
region in the exhaust gas flowing into the SOx trap 11 where the
air-fuel ratio locally becomes very rich will be formed. Therefore,
there is a high possibility that the temperature of the SOx trap 11
will locally become higher than the SOx release temperature.
Therefore, when executing NOx release control, if the lean degree
of the air-fuel ratio of the exhaust gas exhausted from each
cylinder is smaller than the predetermined lean degree, to reliably
keep the SOx trap 11 from releasing SOx, formation of a region in
the exhaust gas where the air-fuel ratio locally becomes very rich
is suppressed. Therefore, it is necessary to keep the temperature
of the SOx trap 11 from locally becoming higher than the SOx
release temperature. Thus, in the NOx release control of the 17th
embodiment, when the lean degree of the air-fuel ratio of the
exhaust gas exhausted from each cylinder is smaller than the
predetermined lean degree, one of the SOx release suppression/NOx
release control of the first embodiment to sixth embodiment is
executed.
[0141] In this regard, as the PM removal control of the exhaust
purification system of the 18th embodiment, the following control
may be employed. That is, in the PM removal control of the 18th
embodiment, when the lean degree of the air-fuel ratio of the
exhaust gas exhausted from each cylinder is larger than a
predetermined lean degree (hereinafter referred to as "the
predetermined lean degree"), one of the ordinary PM removal control
of the seventh embodiment to 14th embodiment is executed when the
PM removal condition stands. On the other hand, when the lean
degree of the air-fuel ratio of the exhaust gas exhausted from each
cylinder is smaller than the predetermined lean degree, one of the
SOx release suppression/PM removal control of the seventh
embodiment to the 14th embodiment is executed when the PM removal
condition stands. According to this, the SOx trap 11 is reliably
kept from releasing SOx.
[0142] That is, when the lean degree of the air-fuel ratio of the
exhaust gas exhausted from each cylinder is smaller than the
predetermined lean degree, the air-fuel ratio of the exhaust gas
becomes close to a rich air-fuel ratio. At this time, if PM removal
control is executed, there is a high possibility that a region in
the exhaust gas flowing into the SOx trap 11 where the air-fuel
ratio locally becomes very rich will be formed. Therefore, when
executing PM removal control, if the lean degree of the air-fuel
ratio of the exhaust gas exhausted from each cylinder is smaller
than the predetermined lean degree, to reliably keep the SOx trap
11 from releasing SOx, formation of a region in the exhaust gas
where the air-fuel ratio locally becomes very rich has to be
suppressed. Therefore, in the PM removal control of the 18th
embodiment, when the lean degree of the air-fuel ratio of the
exhaust gas exhausted from each cylinder is smaller than the
predetermined lean degree, one of the SOx release suppression/NOx
release control of the seven embodiment to 14th embodiment is
executed.
[0143] Note that in the PM removal control of the 18th embodiment,
it is also possible to prohibit execution of the PM removal control
when the lean degree of the air-fuel ratio of the exhaust gas
exhausted from each cylinder is smaller than the predetermined lean
degree. This also enables the SOx trap 11 to be reliably kept from
releasing SOx.
[0144] Further, the NOx release control and PM removal control of
the above-mentioned embodiments can also be applied to the
compression ignition type of internal combustion engine shown in
FIG. 13. The internal combustion engine shown in FIG. 13 is similar
to the internal combustion engine shown in FIG. 1, but in the
internal combustion engine shown in FIG. 13, instead of the NOx
catalyst 12 carried on the filter 12a, a particulate filter 12a for
trapping particulate matter is arranged downstream of the SOx trap
11 and an NOx catalyst 12 is arranged downstream of the particulate
filter 12a. Further, in the internal combustion engine shown in
FIG. 13, when trying to make the NOx absorbent of the NOx catalyst
12 release NOx, the NOx release control of the above-mentioned
embodiments is adopted. Further, in the internal combustion engine
shown in FIG. 13, when trying to burn off the particulate matter
built up on the particulate filter 12a, the PM removal control of
above-mentioned embodiments is employed.
[0145] Note that in the internal combustion engine shown in FIG.
13, the particulate filter 12a is provided with a temperature
sensor 22 for detecting the temperature of the particulate filter
12a and a differential pressure sensor 23 for detecting the
differential pressure before and after the particulate filter 12a.
Further, the NOx catalyst 12 is provided with a temperature sensor
24 for detecting the temperature of the NOx catalyst 12.
[0146] Further, the NOx release control and PM removal control of
the above-mentioned embodiments may also be applied to the
compression ignition type of internal combustion engine shown in
FIG. 14. The internal combustion engine shown in FIG. 14 is similar
to the internal combustion engine shown in FIG. 1, but in the
internal combustion engine shown in FIG. 14, downstream of the SOx
trap 11, instead of the NOx catalyst 12 carried on the filter 12a,
an NOx catalyst 12 is arranged and, downstream of the NOx catalyst
12, just a particulate filter 12a for trapping particulate matter
is arranged. Further, in the internal combustion engine shown in
FIG. 14, when trying to make the NOx absorbent of the NOx catalyst
12 release NOx, the NOx release control of the above-mentioned
embodiments is employed. Further, in the internal combustion engine
shown in FIG. 14, when trying to burn off the particulate matter
built up on the particulate filter 12a, the PM removal control of
the above-mentioned embodiments is employed.
[0147] Further, in the internal combustion engine shown in FIG. 1,
as shown in FIG. 15, it is also possible to arrange upstream of the
SOx trap 11 an oxidation catalyst 26 oxidizing the HC fed from the
HC feed valve 14 into the exhaust gas and provided with an
oxidizing ability higher than the oxidizing ability of the SOx trap
11. In this case, the HC fed from the HC feed valve 14 into the
exhaust gas is oxidized by the oxidation catalyst 26, so formation
of a region in the exhaust gas where the air-fuel ratio locally
becomes rich is reliably suppressed.
[0148] Further, in the exhaust purification system of the
above-mentioned embodiment, the HC feed valve 14 is provided with a
heater for heating the HC feed valve 14. In ordinary NOx release
control or ordinary PM removal control, when the HC feed valve 14
feeds HC into the exhaust gas, the HC feed valve 14 is not heated
by the heater, but in SOx release suppression/NOx release control
or SOx release suppression/PM removal control, when the HC feed
valve 14 feeds HC into the exhaust gas, the HC feed valve 14 may be
heated by the heater. According to this, in SOx release
suppression/NOx release control or SOx release suppression/PM
removal control, HC fed from the HC feed valve 14 easily diffuses
in the exhaust gas, so SOx is kept from being released from the SOx
trap 11.
[0149] Further, in the SOx release suppression/NOx release control
or SOx release suppression/PM removal control of the
above-mentioned embodiments, the pressure for feeding HC from the
HC feed valve 14 into the exhaust gas may be made higher than the
pressure for feeding HC from the HC feed valve 14 into the exhaust
gas in ordinary NOx release control or ordinary PM removal control.
Due to this as well, in SOx release suppression/NOx release control
or SOx release suppression/PM removal control, the HC fed from the
HC feed valve 14 becomes-able to easily diffuse in the exhaust gas,
so SOx is kept from being released from the SOx trap 11.
[0150] Further, in the exhaust purification system of the
above-mentioned embodiment, as the HC feed valve 14, an HC feed
valve provided with a plurality of feed ports for feeding HC and
enabling the number of feed ports feeding HC to be suitably changed
is employed. In the SOx release suppression/NOx release control or
SOx release suppression/PM removal control, when the HC feed valve
feeds HC into the exhaust gas, the number of feed ports for feeding
HC may be made greater than the number of feed ports feeding HC in
ordinary NOx release control or ordinary PM removal control. Due to
this as well, in SOx release suppression/NOx release control or SOx
release suppression/PM removal control, the HC fed from the HC feed
valve 14 becomes able to easily diffuse in the exhaust gas, so SOx
is kept from being released from the SOx trap 11.
[0151] Further, several of the NOx release control methods of the
plurality of the above-mentioned embodiments may be combined within
a range not giving rise to any contradictions, while several of the
PM removal control methods of the plurality of the above-mentioned
embodiments may be combined within a range not giving rise to any
contradictions.
[0152] Further, the NOx release control or PM removal control of
the embodiments other than the above-mentioned second embodiment,
third embodiment, eighth embodiment, and ninth embodiment can be
applied not only to an internal combustion engine feeding HC from
the HC feed valve 14 into the exhaust gas, but also to an internal
combustion engine injecting fuel from a fuel injector 3 in a latter
half of an expansion stroke or during an exhaust stroke of a
specific cylinder.
[0153] Note that the present invention was explained based on
specific embodiments, but a person skilled in the art could make
various changes, modifications, etc. without departing from the
claims and idea of the present invention.
DESCRIPTION OF REFERENCES
[0154] 11. SOx trap [0155] 12. NOx catalyst [0156] 12a. Particulate
filter [0157] 14. HC feed valve
* * * * *