[0001] The Invention relates to a Method to regenerate a particulate filter, in particular
a Diesel paticulate filter (DPF), whereby the particulate filter is arranged in an
exhaust passage for receiving an exhaust gas from an internal combustion engine, in
particular from a Diesel engine, whereby the particulate filter traps particulates
included in the exhaust gas, so that soot is collected inside the particulate filter.
[0002] Methods to regenerate particulate filters, in particular Diesel particulate filters
are known in prior art.
[0003] The
EP 0 528 289 B1 relates to a device for removing particulates in the exhaust gas of a diesel engine.
The device comprises a filter arranged in an exhaust line for receiving the exhaust
gas from the diesel engine, the filter being capable of trapping particulates included
in the exhaust gas. The device further comprises heating means arranged adjacent to
the filter for generating heat in the filter. Further air supplying means for supplyng
air into the filter for incinerating the particulates , and control means for controlling
an amount of air flow for obtaining a desired incineration performance of the particulates
trapped in the filter are comprised by the device. The control means comprises detecting
means for detecting the amount of residual unburnt particulates upon the incineration
process, and air flow amount control means responsive to the detected amount of residual
unburnt particulates for controlling the amount of the air flow used in the subsequent
incineration process.
[0004] The
EP 0 528 289 B1 discloses a device for purifying particulates in the exhaust gas of a diesel engine,
whereby the control means comprises effective area detecting means for detecting the
value of the effective area of the filter before commencement of trapping of the particulates
by the filter, and determining means for determining the amount of the air to be introduced
into the filter in the subsequent incineration process in accordance with the detected
value of the effective area.
[0005] The
EP 0 528 289 B1 describes that during a filter regeneration the periphery of the filter may not be
regenerated completely, leading to a more and more clogged filter after regeneration.
In order to regenerate the DPF additional hardware is used. In the
EP 0 528 289 B1 it is disclosed, that in the centre of the filter a temperature of 900°C is to be
achieved, so that in the periphery a temperature of 500°C is achieved. These high
temperature gradients will certainly decrease filter life time, and limit the soot
load, which in turn will lead to the requirement of more frequent regenerations and
hence a larger fuel consumption.
[0006] The additional hardware, like for example the heating device, the secondary air system,
including an air pump adds hardware costs, takes up package space and uses a lot of
energy, leading to a high operating cost.
[0007] Further disadvantage of the
EP 0 528 289 is to be seen in the fact, that a by-pass valve is used in order to lead exhaust
gases to the environment without passing through the filter, which will lead to emissions
of particulates during all the time when the by-pass is activated.
[0008] Although the
EP 0 528 289 B1 uses pressure difference measurements for determining the amount of soot present
in the filter, no information is available on the axial distribution of the soot after
a (partial) regeneration.
[0009] Therefore the objective of the present invention is to provide a better method to
regenerate a particulate filter which achieves a complete and fast, preferentially
in a short time, regeneration of the particulate filter, thus saving energy, leading
to a low fuel penalty for a driver of a vehicle without using additional hardware
so that extra hardware costs, package space and total vehicle mass is saved leading
to a more robust design.
[0010] The objective is solved by the steps: Initiating an ignition of soot inside the particulate
filter, and actuating a reduction of the exhaust gas mass flow through the filter,
whereby the a.m. steps are repeated several times with a determined frequency so that
a desired degree of filter regeneration is achieved.
[0011] Initiating an ignition of soot inside a filter can be performed by increasing temperature
of the filter utilizing in-cylinder combustion using multiple injections, and/or by
increasing engine speed and/or load, and/or by using post-cylinder fuel or other combustible
compound injection/addition into the post-combustion gases and burning this combustible
compound over an oxidation catalyst placed in the exhaust gas passage between combustion
chamber(s) and (diesel) particulate filter, or over an active catalyst deposited onto
the (diesel) particulate filter material.
[0012] To detect the initiation of soot combustion inside a filter, monitoring means such
as measurements of the exhaust gas mass flow, fuel consumption, exhaust gas and internal
filter temperatures, exhaust gas backpressure, can be applied.
[0013] In a first embodiment reducing the exhaust gas mass flow through the filter, preferentially
together with increasing concentration of oxygen in the exhaust gas, can be done by
means of switching the engine into conditions providing lower mass flow and/or higher
oxygen content (for example idling), if necessary ― together with decreasing amount
of fuel added for heating a particulate filter.
[0014] In a second embodiment reducing the exhaust gas mass flow through the filter, preferentially
together with increasing concentration of oxygen in the exhaust gas, can be done by
means of activating valve(s) allowing only a controllable portion of the exhaust gas
to pass through the filter, while the rest of the exhaust gas to by-pass the filter,
if necessary - together with decreasing amount of fuel added for heating a particulate
filter.
[0015] In a third embodiment reducing the exhaust gas mass flow through the filter, preferentially
together with increasing concentration of oxygen in the exhaust gas, can be done by
means of activating a system that separately supplies air and/or exhaust gas to the
filter at flow rate and with oxidant content that are sufficient to maintain the filter
regeneration.
[0016] In the following some examples of results by using the inventional method are shown.
The used abbreviations in the respective tables are defined as:
SL, g/L- |
Soot loading, gram/liter, |
DPF- |
Diesel Particulate Filter, |
SiC- |
silicon carbide (filter material) |
5.66"D x 6" L- |
DPF diameter (D) and length (L) in inches, |
200 cpsi- |
number of cells per square inch, |
[0017] Example 1 a shows versus example 1 b (Table 1), that initiating regeneration during
2 min of post-injecting, followed by decreasing gas flow through a filter together
with cutting off fuelling results in high regeneration efficiency (96%); while without
decreasing gas flow and without cutting fuelling off, similar regeneration efficiency
can be achieved only after 10 min of post injection causing higher fuel consumption
compared to 1a.
Table 1
Ex. No. |
Particulate Filter |
Description |
SL, g/L |
Duration of post injection, s |
Regeneration method and media |
Regeneration efficiency, % mass |
1 a |
DPF#1 |
Catalysed SiC filter; 5,66"D x 6"L; 200cpsi |
8.5 |
123 |
Exhaust gas; after cutting post-injection, mass flow of 30+/-20 kg/hr |
96 |
1 b |
DPF#1 |
Catalysed SiC filter; 5,66"D x 6"L; 200cpsi |
7.5 |
300" |
Exhaust gas; 600°C upstream of the filter continuously during 15 min with post-injection,
mass flow of 90+/-10 kg/hr |
55% |
-*- |
600" |
90% |
-*- |
900" |
100% |
[0018] Example 1a shows versus example 1c (Table 2), that initiating regeneration during
2 min of post-injecting, followed by decreasing gas flow through a filter results
in high regeneration efficiency (96%); with cutting fuelling off but without decreasing
gas flow, regeneration efficiency is much lower (only 27%).
Table 2
Ex. No. |
Particulate Filter |
Description |
SL, g/L |
Duration of post injection, s |
Regeneration method and media |
Regeneration efficiency, % mass |
1 a |
DPF#1 |
Catalysed SiC filter; 5,66"D x 6"L; 200cpsi |
8.5 |
123 |
Exhaust gas; after cutting post-injection, mass flow of 30+/-20 kg/hr |
96 |
|
|
|
|
|
|
|
1c |
DPF#1 |
Catalysed SiC filter; 5,66"D x 6"L; 200cpsi |
7.6 |
123 |
Exhaust gas; before and after cutting post- injection, mass flow of 90+/-10 kg/hr |
27 |
[0019] Examples 2a and 2b (Table 3) show that according to the method of the present invention,
either exhaust gas, or air can be used for efficient regeneration of a particulate
filter.
Table 3
Ex. No. |
Particulate Filter |
Description |
SL, g/L |
Duration of post injection, s |
Regeneration method and media |
Regeneration efficiency, % mass |
2a |
DPF#2 |
Catalysed SiC filter; 5,66"D x 6"L; 300cpsi |
6.3 |
119 |
Exhaust gas; after cutting post-injection, mass flow of 30+/-20 kg/hr |
69.5 |
2b |
DPF#2 |
Catalysed SiC filter; 5,66"D x 6"L; 300cpsi |
6.7 |
115 |
After cutting post-injection, air with mass flow of 30+/-20 kg/hr |
71.1 |
[0020] Examples 3a-3e (Table 4) show that the method of the present invention is applicable
to un-catalysed filters
Table 4
Ex. No. |
Particulate Filter |
Description |
SL, g/L |
Duration of post injection, s |
Regeneration method and media |
Regeneration efficiency, % mass |
3a |
DPF#3 |
Uncoated SiC; 5,66"D x 6"L; 200 cpsi |
3.40 |
172 |
Exhaust gas; after cutting post-injection, mass flow of 30+/-20 kg/hr |
94.0 |
3b |
-"- |
-"- |
5.40 |
175 |
-"- |
90.9 |
3c |
-"- |
-"- |
8.43 |
130 |
-"- |
74.3 |
3d |
-"- |
-"- |
11.30 |
123 |
-"- |
65.9 |
3e |
-"- |
-"- |
12.69 |
121 |
-"- |
67.7 |
[0021] Examples 4a-4g (Table 5) show that the method of the present invention is applicable
to processes in which regeneration is assisted by fuel borne additive.
Table 5
Ex. No. |
Particulate Filter |
Description |
SL, g/L |
Duration of post injection, s |
Regeneration method and media |
Regeneration efficiency, % mass |
4a |
DPF#4 |
Uncoated SiC X00 cpsi; 5,66"D x 10"L; Ce-Fe fuel borne additive assisted regeneration |
3.95 |
126 |
Exhaust gas; after cutting post-injection, mass flow of 30+/-20 kg/hr |
90.8 |
4b |
-"- |
-"- |
5.02 |
70 |
-"- |
98.1 |
4c |
-"- |
-"- |
5.77 |
84 |
-"- |
93.3 |
4d |
-"- |
-"- |
7.98 |
40 |
-"- |
97.3 |
4e |
-"- |
-"- |
9.70 |
66 |
-"- |
95.8 |
4f |
-"- |
-"- |
11.45 |
70 |
-"- |
96.0 |
4g |
-"- |
-"- |
14.12 |
51 |
|
96.0 |
[0022] Examples 5a-5d (Table 6) show that the method of the present invention is applicable
to the catalysed DPF prepared on the silicon carbide 200 cpsi DPF support (6"-long
filter).
Table 6
Ex. No. |
Particulate Filter |
Description |
SL, g/L |
Duration of post injection, s |
Regeneration method and media |
Regeneration efficiency, % mass |
5a |
DPF #5 |
Catalysed SiC filter; 5,66"D x 6"L; 200cpsi |
4.6 |
116 |
Exhaust gas; after cutting post-injection, mass flow of 30+/-20 kg/hr |
45.5 |
5b |
-"- |
-"- |
5.8 |
156 |
-"- |
100 |
5c |
-"- |
-"- |
8.5 |
157 |
-"- |
97.6 |
5d |
-"- |
-"- |
9.7 |
147 |
-"- |
93.6 |
[0023] Examples 6a-6g (Table 7) show that the method of the present invention is applicable
to the longer catalysed filters; in this case, results for DPF prepared on the silicon
carbide 300 cpsi DPF support are shown (10"-long filter).
Table 7
Ex. No. |
Particulate Filter |
Description |
SL, g/L |
Duration of post injection, s |
Regeneration method and media |
Regeneration efficiency, % mass |
6a |
DPF #6 |
Catalysed SiC filter; 5,66"D x 10"L; 300cpsi |
3.7 |
101 |
Exhaust gas; after cutting post-injection, mass flow of 30+/-20 kg/hr |
50.0 |
6b |
-"- |
-"- |
5.2 |
117 |
-"- |
68.2 |
6c |
-"- |
-"- |
5.7 |
156 |
-"- |
88.1 |
6d |
-"- |
-"- |
7.0 |
173 |
-"- |
100 |
6e |
-"- |
-"- |
7.8 |
117 |
-"- |
79.6 |
6f |
-"- |
-"- |
9.0 |
101 |
-"- |
91.4 |
6g |
-"- |
-"- |
10.2 |
96 |
-"- |
100 |
[0024] Examples 7a-7g (Table 8) show that the method of the present invention is applicable
to even much longer catalysed filters; in this case, results for DPF prepared on the
silicon carbide 300 cpsi DPF support are shown (14"-long filter).
Table 8
Ex. No. |
Particulate Filter |
Description |
SL, g/L |
Duration of post injection, s |
Regeneration method and media |
Regeneration efficiency, % mass |
7a |
DPF #7 |
Catalysed SiC filter; 5,66"D x 14"L; 300cpsi |
4.2 |
96 |
Exhaust gas; after cutting post-injection, mass flow of 30+/-20 kg/hr |
61.3 |
7b |
-"- |
-"- |
4.9 |
100 |
-"- |
45.7 |
7c |
-"- |
-"- |
6.2 |
104 |
-"- |
48.1 |
7d |
-"- |
-"- |
6.5 |
139 |
-"- |
89.5 |
7e |
-"- |
-"- |
7.6 |
136 |
-"- |
92.1 |
7f |
-"- |
-"- |
8.7 |
129 |
-"- |
95.7 |
7g |
-"- |
-"- |
9.6 |
115 |
-"- |
99.1 |
[0025] Examples 8a-8d (Table 9) show that the method of the present invention is applicable
to the catalysed DPF prepared on the refractory oxide (cordierite) 300 cpsi DPF support
(6"-long filter).
Table 9
Ex. No. |
Particulate Filter |
Description |
SL, g/L |
Duration of post injection, s |
Regeneration method and media |
Regeneration efficiency, % mass |
8a |
DPF #8 |
Catalysed SiC filter; 5,66"D x 6"L; 300cpsi |
2.0 |
116 |
Exhaust gas; after cutting post-injection, mass flow of 30+/-20 kg/hr |
81.3 |
8b |
-"- |
-"- |
3.8 |
133 |
-"- |
66.7 |
8c |
-"- |
-"- |
6.2 |
99 |
-"- |
88.2 |
8d |
-"- |
-"- |
7.5 |
97 |
-"- |
94.0 |
[0026] As the above examples show, each regeneration carried out via the inventional method
provides nearly complete regeneration of the particulate filter. Mainly insulated
particulate filters and particulate filters with a high thermal conductivity are used,
so that radial temperature profiles are reduced. The reduced radial temperature profiles
lead advantageously to an increased particulate filter lifetime and hence a smaller
fuel consumption.
[0027] Advantageously only an engine calibration is required, which can be fully controlled
by a known motor management system, so that no extra package space and hardware costs
is used. Even the energy required for heating the particulate filter is reduced.
[0028] Because of the fact, that the exhaust gases in the preferred embodiment pass through
the particulate filter at every time, even during regeneration, emissions to the environment
are reduced.
[0029] With the inventional method a complete and fast regeneration of the particulate filter
is achieved, thus saving energy, leading to a low fuel penalty for the driver. The
complete regeneration can be achieved within a short time, saving extra hardware costs,
saving package space and total vehicle mass, leading to a more robust design since
the method is implemented fully in the motor management system.
[0030] The preferred embodiment of the invention includes, after initiating particulate
regeneration inside the filter, putting the engine into low mass-flow and/or higher
oxygen content conditions to support regeneration without any other means such as
secondary air supply, external heater, additional valves, pipes or by-passes.
1. Method to regenerate a particulate filter, in particular a Diesel paticulate filter
(DPF), whereby the particulate filter is arranged in an exhaust passage for receiving
an exhaust gas from an internal combustion engine, in particular from a Diesel engine,
whereby the particulate filter traps particulates included in the exhaust gas, so
that soot is collected inside the particulate filter
characterized by
the steps of (i) initiating an ignition of soot inside the particulate filter, and
(ii) actuating a reduction of the exhaust gas mass flow through the filter, whereby
the steps (i) and (ii) can be repeated several times with a determined frequency so
that a desired degree of filter regeneration is achieved.
2. Method according to claim 1,
characterized in, that
the initiating of the ignition of soot inside the (diesel) particulate filter is performed
by increasing temperature of the (diesel) particulate filter by in-cylinder combustion
with multiple post injections.
3. Method according to claim 1 or 2,
characterized in, that
the initiating of the ignition of soot inside the (diesel) particulate filter is performed
by increasing temperature of the (diesel) particulate filter by increasing engine
speed and/or load.
4. Method according to one of the preceding claims,
characterized in, that
the initiating of the ignition of soot inside the (diesel) particulate filter is performed
by increasing temperature of the (diesel) particulate filter by combustible compound
injection into post combustion gases and burning the said combustible compound over
an oxidation catalyst placed in the exhaust gas passage between combustion chamber(s)
and the (diesel) particulate filter.
5. Method according to claim 4,
characterized in, that
the combustible compound preferably is normal fuel.
6. Method according to one of the preceding claims,
characterized by
monitoring means in order to detect the initiation of soot combustion inside the (diesel)
particulate filter.
7. Method according to one of the preceding claims,
characterized in, that
the exhaust gas mass flow through the (diesel) particulate filter is reduced preferentially
with increasing concentration of oxygen in the exhaust gas, by means of switching
the engine into conditions providing lower mass flow.
8. Method according to one of the preceding claims,
characterized in, that
the exhaust gas mass flow through the (diesel) particulate filter is reduced preferentially
with increasing concentration of oxygen in the exhaust gas, by means of switching
the engine into conditions providing higher oxygen content.
9. Method according to one of the preceding claims,
characterized in, that
the exhaust gas mass flow through the (diesel) particulate filter is reduced preferentially
with increasing concentration of oxygen in the exhaust gas, by means of activating
a system that separately supplies air to the (diesel) particulate filter at flow rate
and with oxidant content that are sufficient to maintain the (diesel) particulate
filter regeneration.
10. Method according to one of the preceding claims,
characterized in, that
the exhaust gas mass flow through the (diesel) particulate filter is reduced preferentially
with increasing concentration of oxygen in the exhaust gas, by means of activating
a system that separately supplies exhaust gas to the (diesel) particulate filter at
flow rate and with oxidant content that are sufficient to maintain the (diesel) particulate
filter regeneration.