Technical Field
[0001] The present invention relates to an exhaust gas treatment technique for large-displacement
diesel engines using particularly a low-grade fuel equal to or less than fuel oil,
such as for watercrafts, for power generation, or for industrial purposes, for eliminating
particulate matter (called below "PM") mainly composed of carbon, or harmful gas,
contained in exhaust gas of a diesel engine to purify the exhaust gas, and, in particular,
relates to an exhaust gas treatment equipment using corona discharge in the large-displacement
diesel engine exhausting high-temperature exhaust gas.
Background Art
[0002] Diesel engines are widely adopted as power sources for various watercrafts, power
generators, large construction machines, and further, various automobiles, but since
the PM contained in exhaust gas exhausted from the diesel engines, as is well known,
not only causes air pollution, but also is extremely harmful to human bodies, purification
of the exhaust gas is extremely important. Therefore, many suggestions have already
been made, such as improvement of combustion systems of diesel engines, adoption of
various types of exhaust gas filters, or electrical treatment methods using corona
discharge, and some of such suggestions have been in practical use.
[0003] Here, the components of the PM (particulate matter) in the exhaust gas of the diesel
engine can be classified into two components: soluble organic fractions (called below
"SOF"); and insoluble organic fractions (called below "ISF"), and the SOF of the two
components is mainly composed of unburnt combustion components of fuel or lubricant
oil, and including harmful matter such as carcinogenic polycyclic aromatics. On the
other hand, the ISF is mainly composed of low electrical resistive carbon (soot) and
sulfate components, and the exhaust gas is desired to have as small an amount of SOF
and ISF as possible, because of the effects of the SOF and ISF on human bodies and
the environment. In particular, it is also said that the degree of the harmful effect
of the PM on human bodies is problematic especially when the particulate size becomes
nanometer size.
[0004] As the electrical treatment method using corona discharge, for example, the methods
and equipments (patent literatures 1 to 5) described below have been suggested.
[0005] That is, as shown briefly in FIG. 12, the patent literature 1 suggests an electrical
treatment method and equipment for exhaust gas of a diesel engine, the method and
equipment having a system in which a discharging and charging part 22 comprising a
corona discharging part 22-1 and a charging part 22-2 is so provided as to communicate
with an exhaust gas passage 21, PM 28 mainly composed of carbon in exhaust gas G1
is charged with corona-discharged electrons 29, and the charged PM 28 is collected
by a collection plate 23 disposed in the exhaust gas passage 21, the method and equipment
having a configuration in which the length of an electrode needle 24 in the discharging
and charging part 22 is short in a flowing direction of an exhaust gas stream, and
the collection plate 23 is disposed so as to be perpendicular to the flowing direction
of the exhaust gas stream. In FIG. 12, the reference numeral 25 denotes a seal gas
pipe, 26 high-voltage power supply apparatus, and 27 an exhaust gas guide pipe.
[0006] In addition, as shown briefly in FIG. 13, the patent literature 2 suggests diesel-engine
exhaust gas PM collector comprising a needle electrode 31 for causing corona discharge
35 around a needle tip 31-1 to charge PM 33 in exhaust gas, a collecting electrode
32 for collecting the charged PM 33, and a high-voltage DC power supply 34 for applying
a predetermined DC high voltage to between the needle electrode 31 and the collecting
electrode 32. In FIG. 13, the reference numeral 36 denotes a deflection electrode.
[0007] Further, as shown briefly in FIG. 14, the patent literature 3 suggests an exhaust
gas purification equipment comprising a stationary cylindrical body 41 constituting
one of a pair of collection electrodes for collecting PM provided in an exhaust gas
route, an electrode bar 42 being extended axially in the center of the stationary
cylindrical body 41 and constituting the other of the pair of the collection electrodes,
a high-voltage power source part 43 forming an electrostatic field between the pair
of collection electrodes and accumulating the PM in the exhaust gas on an inner face
of the stationary cylindrical body 41, and a scraping-off part 44 making rotational
movement relative to the stationary cylindrical body along the inner face of the stationary
cylindrical body 41 and scraping off the PM accumulated on the inner face of the stationary
cylindrical body. In FIG. 14, the reference numeral 45 denotes a discharge pipe, and
46 a rotary cylindrical part.
[0008] On the other hand, the patent literature 4 suggests a diesel-engine exhaust gas purification
equipment comprising an electrical precipitation means having a discharge electrode
charging PM contained in exhaust gas of a diesel engine and a precipitation electrode
collecting the charged PM, a means for detaching the PM collected and retained on
the precipitation electrode from the particulate electrode, and a cyclone-system segregating
and collecting means for segregating and collecting the PM detached from the precipitation
electrode.
This equipment, as shown by way of example in FIG. 15, is configured to treat the
exhaust gas while causing the exhaust gas to flow laterally, and comprises an electrical
precipitation part 51 for collecting the PM, and a cyclone 52 serving as a segregating
and collecting part, where the electrical precipitation part 51 comprises: a precipitation
electrode 54 composed of a tubular metal body 57 attached to an inner peripheral face
of a tubular housing 56 and an uneven part 58 formed on an inner peripheral face of
the tubular metal body; and a discharge electrode 55 composed of a main electrode
59 extending along the axial line of the precipitation electrode 54 and a group of
radially-projecting electrode needles 60 disposed at predetermined intervals in a
longitudinal direction of the main electrode 59, and the cyclone 52 is configured
downstream from a guide vane 61 converting a gas stream 53 which has passed through
the electrical precipitation part 51 into a swirling flow, and an exhaust pipe 62
for discharging gas in the cyclone and a hopper 63 collecting the PM separated by
centrifugation are provided downstream from the cyclone 52. The reference numeral
64 denotes a detaching mechanism detaching the PM collected and retained on the precipitation
electrode 54 from the precipitation electrode, and composed of an eccentric motor
65 generating vibration due to eccentricity, for example. The reference numeral 66
denotes a gas-extraction pipe for returning the exhaust gas in the exhaust pipe 62
to an upper space of the hopper 63.
In other words, the exhaust gas purification equipment thus configured has an arrangement
in which the PM in the exhaust gas which has flowed into the electrical precipitation
part 51 is charged by discharge between the precipitation electrode 54 and the discharge
electrode 55 to be collected on the precipitation electrode 54 by coulomb force, then
the collected PM flows into the guide vane 61 with the gas stream, then the PM is
centrifugally separated by the cyclone 52 configured downstream from the guide vane
61, and then the centrifugally-separated PM falls down to the hopper 63 and is collected,
while the purified exhaust gas is released outside via the exhaust pipe 62.
[0009] In addition, the patent literature 5 suggests a gas treatment equipment comprising
a charging and agglomerating part for charging and agglomerating, by corona discharge,
target components to be collected in exhaust gas of a diesel engine mounted on an
automobile, and a filter part for collecting the agglomerated components, the gas
treatment equipment. As shown in FIGS. 16 and 17, this gas treatment equipment has
a configuration in which the charging and agglomerating part 70 is disposed upstream,
and the filter part 80 is disposed downstream, a gas passage wall of the charging
and agglomerating part 70 is formed of tubular bodies 71, 71a, etc., a precipitation
electrode, which is a low-voltage electrode, is formed of a conductive tubular body
71f disposed in the vicinity of the surface of the gas passage wall, corona electrodes
are formed of wire-like high-voltage electrodes disposed inside these tubular bodies,
and the tubular body of the gas passage wall is formed as a gas cooling part where
natural convection and heat radiation cool gas naturally, and further a turbulence
promoting means 71e for promoting disturbance of a gas stream passing in the vicinity
of an inner surface of the tubular body of the gas passage wall or the conductive
tubular body is provided on the surface of the tubular body or in the vicinity of
the surface thereof. In FIGS. 16 and 17, the reference numeral 71c denotes a gas intake
chamber, 71b a corona electrode, and 71d a gas outlet chamber.
Citation List
Patent Literature
Summary of Invention
Technical Problem
[0011] However, the above-described conventional diesel-engine exhaust gas purification
equipments have the following drawbacks.
That is, the electrical treatment method and equipment for exhaust gas of a diesel
engine described in the patent literature 1 has problems as follows: high flow resistance
(pressure loss) due to the configuration in which the length of the electrode needle
24 in the discharging and charging part 22 is short in the flowing direction of the
exhaust gas stream and the collection plate 23 is so disposed as to be perpendicular
to the flowing direction of the exhaust gas stream, and in which the exhaust gas stream
directly hits the collection plate 23; a possibility that since the collection plate
23 is thin and short in length in the flowing direction of the exhaust gas stream,
the PM might pass through the collection plate 23 and the PM collection efficiency
thus could not sufficiently be increased; and a worry that once the PM passes through
the collection plate 23, the PM may not be charged by corona discharge or collected
again, and may be exhausted as it is.
It should be noted that the patent literature 1 neither discloses nor suggests the
technical idea that the collection plate has a tubular shape which is long in the
flowing direction of the exhaust gas stream, the electrode needle is disposed in an
axial direction of the tubular collecting part, a jumping phenomenon of depositing
and detaching repeatedly the PM particles flowing in the flowing direction of the
exhaust gas stream is caused so that the PM is grown, this growth phenomenon causes
the size of the PM in the exhaust gas stream in the vicinity of an inner face of the
tubular collecting part to increase so that a cyclone can easily collect the PM, and
causes the PM concentration to increase, and this exhaust gas stream having the large-size
PM and the high PM concentration is selectively extracted and then the PM is collected
by the cyclone.
[0012] In addition, the exhaust gas PM collecting apparatus described in the patent literature
2 and the exhaust gas purification equipment described in the patent literature 3
have drawbacks as follows: a difficulty in setting both the discharge voltage and
the collecting deflection voltage at their respective appropriate conditions due to
the fact that the voltages are the same potential; a requirement that a large space
must be left between the deflection electrode and the collecting electrode in order
to prevent a spark from occurring therebetween; a reduction in collection efficiency
due to an increase in the amount of PM passing through a collecting section without
being collected due to the above requirement; and further, an inevitable increase
in equipment size, which is inappropriate as a marine component that is desired to
be small in size and light in weight, due to a requirement that the volume of the
collecting part must be large in order to raise the collection efficiency.
Besides, the patent literature 2 states that the collecting electrode 32 is formed
as a tunnel-like electrode through which the exhaust gas passes, that a combined-electrode
body composed of the needle electrodes 31 and the deflection electrodes 36 is disposed
in the tunnel of the collecting electrode 32 substantially coaxially with the tunnel,
and that the combined-electrode body, which is thick and long, is disposed in the
tubular collecting part over substantially the entire length thereof and arranged
in a grid-like pattern. And also in the patent literature 3, a tubular collecting
part is formed according to the following statements: "...an electrode bar 42 constituting
one of the discharge electrode pair and one of the collection electrode is hung along
the axis of the stationary cylindrical body 41, ...a wide gas outlet is provided in
a lower side face of the stationary cylindrical body 41, and the gas outlet is fitted
with a downstream exhaust pipe 45..." in paragraph [0033] in Example 6; "the rotary
cylindrical part 46 has the shape of an inverted truncated cone, ...a long bar (scraping
part) 44 extends upward on an inner face of the rotary cylindrical part 46, and an
outer edge of the bar 44 is in contact with an inner face of a wide portion of the
stationary cylindrical body 41." in paragraph [0035]; "...diesel particulates... by
corona discharge between the electrode bar 42 and...the stationary cylindrical part
41 in the discharge space... The charged diesel particulates are attracted by an electrostatic
field and deposited on the inner face of the wide part of the stationary cylindrical
body 41." in paragraph [0036]; and further, "According to the rotation of the rotary
cylindrical part 46, the bar 44 rotates at low speed in contact with the inner face
of the wide part of the stationary cylindrical body 41, and drops a diesel-particulate
layer deposited on the inner face of the wide part... The diesel-particulates are
collected in a collection box... can be eliminated" in paragraph [0037]. But the technique
described in the patent literature 3 is such a technique that the collecting electrode
is provided as a stationary cylindrical portion (tubular) which is long in the flowing
direction of the exhaust gas stream, the electrode needle is disposed with a space
in the axial direction of the tubular collecting part, the PM is deposited flowing
in the flowing direction of the exhaust gas stream, and the deposited PM particles
are scraped off with the bar, and such technique is a technique which is very likely
to discharge some of the PM particles, which fly when the PM particles are scraped
off, from the downstream exhaust pipe fitted in the wide gas outlet port provided
upstream from the collection box.
Therefore, both techniques described in the patent literatures 2 and 3, like the technique
described in the patent literature 1, neither disclose nor suggest the technical idea
that the collection plate has a tubular shape which is long in the flowing direction
of the exhaust gas stream, the electrode needle is disposed in the axial direction
of the tubular collecting part, a jumping phenomenon of depositing and detaching repeatedly
the PM particles flowing in the flowing direction of the exhaust gas stream is caused
so that the PM particles are grown, this growth phenomenon causes the size of the
PM in the exhaust gas stream in the vicinity of an inner face of the tubular collecting
part to increase so that a cyclone can easily collect the PM, and causes the PM concentration
to increase, and the exhaust gas stream having the large-size PM and the high PM concentration
is selectively extracted and the PM is efficiently collected by the cyclone.
[0013] On the other hand, the diesel-engine exhaust gas purification equipment described
in the patent literature 4 has a system in which the PM particles collected on the
precipitation electrode 54 or the inner peripheral wall (collecting pipe wall) of
the tubular housing 56 of the electrical precipitation part 51 are agglomerated into
large masses, then the PM masses are naturally detached or released from the precipitation
electrode 54 or the collecting pipe wall by a mechanical detachment mechanism and
to be mixed in the tubular housing 56, and then the released and mixed PM masses are
separated by centrifugation from the exhaust gas in the cyclone 52 to be collected
again in the hopper 63. But this system has the drawbacks as follows: a high facility
cost and running cost due to the necessity of the large cyclone 52 with the large
guide vane 61 that is inevitably caused by the centrifugation of PM from the whole
amount of the exhaust gas flowing into the cyclone 52 by the guide vane 61 disposed
in the tubular housing 56 and involving mixing of the whole exhaust gas amount; the
incapability of responding to a significant increase or decrease in exhaust gas flow
rate involved in an increase or decrease in the number of operating engines or a large
variation in engine load ratio due to the structural incapability of installing a
plurality of cyclones 52; and the incapability of maintaining a high PM collection
efficiency and solving such a problem as a deterioration in fuel economy due to an
excessive pressure loss in the cyclone due to the lack of a means for controlling
the exhaust gas flow velocity at the cyclone inlet portion appropriately.
In the patent literature 4, the collection plate has a tubular shape which is long
in the flowing direction of the exhaust gas stream, the electrode needle is disposed
in an axial direction of the tubular collecting part, and the PM particles flowing
in the flowing direction of the exhaust gas stream are deposited in the vicinity of
an inner face of the tubular collecting part, and collected by the cyclone, but the
technique described in the patent literature 4, like the techniques described in the
patent literatures 1 to 3, neither discloses nor suggests the technical idea that
the particle size of the PM in the exhaust gas is coarsened so that the cyclone can
easily collect the PM, and the PM concentration of the exhaust gas stream in the vicinity
of the inner face of the tubular collecting part is increased, and further only this
stream of the exhaust gas in the vicinity of the inner face of the tubular collecting
part, which has the PM with the enlarged particle diameters and the high PM concentration,
is selectively extracted and collected by the cyclone in a focused manner.
[0014] Furthermore, the gas treatment equipment described in the patent literature 5 is
a vehicle-mounted small-sized gas treatment equipment, and is directed to a technique
relating to an equipment in which the charging and agglomerating part 70 is configured
to be disposed upstream, and the filter part 80 is disposed downstream, the charging
and agglomerating part 70 is provided with the gas intake chamber 71c branching the
exhaust gas into many streams, the gas passage wall is formed of the tubular body
71f, the tubular body 71f is exposed to ambient air and the tubular body 71f, which
is the gas passage wall, is formed as a gas cooling part cooling the gas by natural
heat loss due to natural convection and heat radiation, and the branched exhaust gas
streams are then mixed again in the gas outlet chamber 71d. Such technique is different
from a technique (the present invention described later) where an exhaust gas stream
flowing from the tubular collecting part is not mixed again before the step of collecting
PM particles. The gas treatment equipment described in the patent literature 5 has
the drawback that since the means 71e for promoting disturbance of the gas stream
is provided on the inner surface of the tubular body 71f or in the vicinity of the
inner surface thereof, the disturbance of the gas is promoted particularly in the
vicinity of the surface of the tubular body, which results in an increased agitating
effect in the cross-sectional direction of the flow passage.
In the equipment described in the patent literature 5, the collecting wall is formed
in a tubular shape which is long in the flowing direction of the exhaust gas stream,
the electrode needle is disposed in an axial direction of the tubular collecting part,
and the PM particles are deposited in the vicinity of an inner face of the tubular
collecting part and collected by the cyclone, while being caused to flow in the flowing
direction of the exhaust gas stream. But the technique described in the patent literature
5, like the techniques described in the patent literatures 1 to 4, neither discloses
nor suggests the technical idea that the particle size of the PM in the exhaust gas
is coarsened so that the cyclone disposed downstream can easily collect the PM and
the PM concentration of the exhaust gas stream in the vicinity of the inner face of
the tubular collecting part is increased, and further only this stream of the exhaust
gas in the vicinity of the inner face of the tubular collecting part, which has the
PM with the large particle diameters and the high PM concentration, is selectively
extracted and collected by the cyclone in a focused manner.
[0015] The present invention has been made in order to solve the drawbacks of the conventional
techniques described above, and it is intended to provide an exhaust gas purification
equipment for a diesel-engine where, in particular, in place of the system of the
diesel-engine exhaust gas purification equipment described in the patent literature
4 wherein the cyclone is constituted by providing a guide vane in the passage through
which the entire amount of the exhaust gas flows, a system is adopted in which a segregating
and collecting means of a cyclone system is disposed not within the tubular collecting
part but on the downstream side of the tubular collecting part, and in which the cyclone
collecting means is composed of a plurality of tangential cyclones, so that it is
possible to reduce the size of the cyclone, and it is also possible to select appropriately
and use the cyclone according to a significant increase or decrease in exhaust gas
flow rate due to a change in operating condition or a large variation in engine load
ratio involved in parallel operation or individual operation of a main engine and
an auxiliary engine in a marine engine, and wherein a means for controlling appropriately
the exhaust gas flow rate at a cyclone inlet portion is further provided, so that
it is possible to maintain a high PM collection efficiency and solve such a problem
as a deterioration in fuel economy due to an excessive pressure loss in the gas purification
equipment.
Solution to Problems
[0016] An exhaust gas treatment equipment for a diesel engine according to the present invention
includes: an electrical precipitation means having a discharge electrode for charging
PM contained in exhaust gas of a diesel engine using a low-grade fuel equal to or
less than fuel oil and a tubular collecting part having a predetermined length and
constituting a precipitation electrode for collecting the PM charged, the discharge
electrode being composed of a main electrode disposed in an axial direction in the
tubular collecting part and a plurality of electrode needles disposed at intervals
on the main electrode and projecting radially; and a segregating and collecting means
of a cyclone system for segregating and collecting the PM which has been detached
from the tubular collecting part, wherein the exhaust gas treatment equipment has
an arrangement in which an exhaust gas outlet pipe for low PM concentration is provided
in the vicinity of an axial center on a downstream side of the tubular collecting
part and an exhaust gas outlet portion for high PM concentration is provided in the
vicinity of an inner peripheral face on the downstream side of the tubular collecting
part, a cyclone collecting means for collecting the PM is provided so as to communicate
with the exhaust gas outlet portion for high PM concentration, the cyclone collecting
means being composed of a tangential cyclone, and the velocity of exhaust gas flowing
into the tangential cyclone is controlled by controlling an opening position of a
damper provided in the exhaust gas outlet pipe for low PM concentration. Obviously,
the low PM concentration of exhaust gas means exhaust gas having a low PM content
(or purified exhaust gas) and the high PM concentration of exhaust gas means exhaust
gas containing much PM.
[0017] The equipment according to the present invention also has a system in which the cyclone
collecting means is composed of a plurality of tangential cyclones so that high PM
concentration of exhaust gas discharged through the exhaust gas outlet portion for
high PM concentration is selectively introduced into the tangential cyclones according
to the flow rate of the high PM concentration of exhaust gas.
[0018] In a preferred aspect, the equipment according to the present invention has a configuration
in which the tubular collecting part has a radially-expanding tubular portion having
a gradually-increasing diameter and a large-diameter tubular portion communicating
with the radially-expanding tubular portion at an end on the downstream side of the
tubular collecting part, and the exhaust gas outlet pipe for low PM concentration
and the exhaust gas outlet portion for high PM concentration are provided, in a communicating
manner, in the vicinity of an axial center of the large-diameter tubular portion and
in the vicinity of an inner peripheral face of the large-diameter tubular portion,
respectively.
[0019] Further, in another preferred aspect, the equipment according to the present invention
has a configuration in which the discharge electrode is provided so as to extend to
the area of the radially-expanding tubular portion or the area of the radially-expanding
tubular portion and the large-diameter tubular portion communicating with the radially-expanding
tubular portion, in the tubular collecting part.
[0020] In another preferred aspect of the equipment according to the present invention,
the cyclone collecting means is composed of a plurality of tangential cyclones having
different treatment capacities, and a flow-rate control damper is provided at an inlet
of each tangential cyclone. In a further preferred aspect, the equipment according
to the present invention has a configuration in which a discharge pipe for causing
purified gas that has passed through the tangential cyclone to flow into the low PM
concentration of exhaust gas is provided between the tangential cyclone and the exhaust
gas outlet pipe for low PM concentration, and an air nozzle or a motor-driven fan
is disposed in the discharge pipe.
[0021] Furthermore, in another preferred aspect of the equipment according to the present
invention, the tubular collecting part is substantially horizontally disposed, the
tubular collecting part is disposed substantially vertically such that the exhaust
gas flows upward, or the tubular collecting part is disposed substantially vertically
such that the exhaust gas flows downward.
Advantageous Effects of Invention
[0022] According to the present invention, since the exhaust gas purification equipment
for a diesel engine adopts a system in which the PM is separated by centrifugation
outside the tubular collecting part, a phenomenon occurs where PM in exhaust gas is
collected on the tubular collecting wall and grown into a mass and this PM mass gradually
increases in PM concentration in the vicinity of the tubular collecting wall while
repeating attachment and detachment to the tubular collecting wall so that an exhaust
gas stream containing PM in high concentration flows downstream, and the exhaust gas
is separated in the tubular collecting part into high PM concentration of exhaust
gas and low PM concentration of exhaust gas having only a low PM concentration due
to gradual decrease in PM concentration in the vicinity of the axial center of the
tubular collecting part, and then the high PM concentration of exhaust gas flows in
the vicinity of the tubular collecting wall and the low PM concentration of exhaust
gas flows in the vicinity of the axial center portion of the tubular collecting part,
which makes it possible to introduce only the high PM concentration of exhaust gas
having a high PM concentration from the vicinity of the tubular collecting wall to
the cyclone collecting means. That is, according to the equipment of the present invention,
only high PM concentration of exhaust gas, which is a part of the entire exhaust gas
amount, can be introduced into the cyclone, and therefore the size of the cyclone
can be reduced. On the other hand, the low PM concentration of exhaust gas having
the decreased PM concentration (or purified exhaust gas) is released outside through
the exhaust gas outlet pipe for low PM concentration provided in a communicating manner
in the vicinity of the axial center on the downstream side of the tubular collecting
part.
[0023] In addition, according to the equipment of the present invention, since a system
is adopted in which the cyclone collecting means is composed of a plurality of tangential
cyclones so that high PM concentration of exhaust gas discharged through the exhaust
gas portion for high PM concentration is selectively introduced into the tangential
cyclones according to the flow rate of the high PM concentration of exhaust gas, it
becomes possible to select an appropriate treatment capacity and the appropriate number
of tangential cyclones according to a significant increase or decrease in the exhaust
gas flow rate due to a change in operating conditions or a large variation in engine
load ratio involved in parallel operation or individual operation of a main engine
and an auxiliary engine in a marine engine, in addition to the functional effect,
"the higher the tangential velocity of a fluid flowing in is, the higher the collection
efficiency becomes", of a tangential cyclone which has a better collection performance
than the axial cyclone of the diesel-engine exhaust gas treatment equipment described
in the patent literature 4 where the guide vane is provided, so that it is possible
to ensure a high PM collection efficiency in response to a change in the exhaust gas
flow rate. Further, since the velocity (tangential velocity) of the exhaust gas flowing
into the tangential cyclone can be appropriately controlled by controlling the opening
position of the damper provided in the exhaust gas outlet pipe for low PM concentration,
it is possible to maintain a high PM collection efficiency and also solve such a problem
as a deterioration in fuel economy due to an excessive pressure loss in the exhaust
gas purification equipment.
[0024] Besides, since the exhaust gas purification equipment for a diesel engine according
to the present invention is provided with a radially-expanding tubular portion having
a gradually-increasing diameter or a large-diameter tubular portion communicating
with the radially-expanding tubular portion on the downstream side of the tubular
collecting part, the high PM concentration of exhaust gas stream is gradually slowed
down due to the radially-expanding tubular portion, so that it is possible to introduce
the PM reliably into the exhaust gas outlet portion for high PM concentration provided
in a communicating manner in the inner peripheral face of the large-diameter tubular
portion. Further, since a configuration is adopted in which the discharge electrode
is provided so as to extend to the vicinity of the inner peripheral face in the area
of the radially-expanding tubular portion and the large-diameter tubular portion communicating
with the radially-expanding tubular portion in the tubular collecting part, it is
possible to collect the PM more effectively, so that the exhaust gas can be further
purified.
[0025] Further, according to the equipment of the present invention, the cyclone collecting
means is composed of a plurality of tangential cyclones having different treatment
capacities, for example, the following three types of cyclones: a tangential cyclone
having a low treatment capacity; a tangential cyclone having an intermediate treatment
capacity; and a tangential cyclone having a high treatment capacity, and a flow-rate
control damper is provided at an inlet of each tangential cyclone, as a result, not
only does it become possible to select and use more appropriately an tangential cyclone
according to a significant increase or decrease in the exhaust gas flow rate due to
a change in operating conditions or a large variation in engine load ratio involved
in parallel operation or individual operation of a main engine and an auxiliary engine
in a marine engine, but it also becomes possible to control the flow-rate control
damper provided for each tangential cyclone in combination with the damper provided
in the exhaust gas outlet pipe for low PM concentration, thereby controlling the velocity
of the exhaust gas flowing into each tangential cyclone more appropriately. In addition,
a configuration is adopted in which a discharge pipe for causing purified gas that
has passed through the tangential cyclone to flow into the low PM concentration of
exhaust gas is provided between the tangential cyclone and the exhaust gas outlet
pipe for low PM concentration, and an air nozzle or a motor-driven fan is disposed
in the discharge pipe, as a result, a purified gas stream which has passed through
the tangential cyclone is accelerated and sucked, so that a pressure loss in the exhaust
gas purification equipment is further improved, which contributes to improvement in
fuel economy.
[0026] Moreover, according to the invention, the following advantages can be obtained: when
the tubular collecting part is disposed substantially horizontally, the workability
at a maintenance time of the collecting pipe, the discharge electrode, and the like
becomes excellent since the tubular collecting part is maintained at a horizontally
substantially constant height from a floor surface of an engine room in which an engine
is placed; when the tubular collecting part is disposed substantially vertically upward,
space saving can be achieved since the tubular collecting part can be double as a
pipe of an exhaust pipe to a funnel; and when the tubular collecting part is disposed
substantially vertically downward, not only it becomes easy to collect the PM falling
down, but also it becomes easy to collect liquefied components because of falling
down the surface of the collecting wall when SOF or sulfate attached to the surface
of the collecting wall is liquefied, , and further it becomes easy to collect even
heavy oxidized scales corroded by sulfate or the like when the scales are detached
and fall down from the surface of the wall.
Brief Description of Drawings
[0027]
Figure 1 is a schematic longitudinal sectional view showing an entire configuration
of a first embodiment equipment of the present invention;
Figure 2 is a schematic longitudinal sectional view showing an entire configuration
of a second embodiment equipment of the present invention;
Figure 3 is a schematic longitudinal sectional view showing in an enlarging manner
an essential portion of a third embodiment equipment of the present invention;
Figure 4 is a schematic longitudinal sectional view showing in an enlarging manner
an essential portion of a modification of the third embodiment equipment of the present
invention;
Figure 5 is a schematic longitudinal sectional view showing in an enlarging manner
an essential portion of a fourth embodiment equipment of the present invention;
Figure 6 is an enlarged sectional view taken along the line a-a in FIG. 5;
Figure 7 is a schematic longitudinal sectional view showing in a partially-omitting
manner an entire configuration of a fifth embodiment equipment of the present invention;
Figure 8 is a descriptive view showing schematically another embodiment of a cyclone
collecting means in the present invention equipment;
Figures 9(a) and 9(b) are descriptive views showing schematically in an enlarging
manner speed-increasing sucking parts of purified gas which has passed through a tangential
cyclone: 9(a) showing an air-nozzle type; and 9(b) showing a motor-driven fan type,
according to in the present invention equipment;
Figure 10 is a schematic view showing an example of disposing a tubular collecting
part in the present invention equipment substantially vertically downward;
Figure 11 is a schematic view showing an example of disposing the tubular collecting
part in the present invention equipment substantially vertically upward;
Figure 12 is a schematic longitudinal sectional view showing an example of conventional
diesel-engine exhaust gas treatment equipment;
Figure 13 is a schematic longitudinal sectional view showing another example of conventional
diesel-engine exhaust gas treatment equipment;
Figure 14 is a schematic longitudinal sectional view showing yet another example of
conventional diesel-engine exhaust gas treatment equipment;
Figure 15 is a schematic longitudinal sectional view showing yet another example of
conventional diesel-engine exhaust gas treatment equipment;
Figure 16 is a schematic longitudinal sectional view showing yet another example of
conventional diesel-engine exhaust gas treatment equipment in a partially-breaking
manner; and
Figure 17 is a partially-enlarged sectional view of the diesel-engine exhaust gas
treatment equipment shown in FIG. 16.
Description of Embodiments
[0028] An exhaust gas treatment equipment for a diesel engine shown as a first embodiment
equipment of the present invention in FIG. 1 is composed of a tubular collecting part
1 constituting an electrical precipitation means and a segregating and collecting
part 2 constituting a segregating and collecting means, which are roughly sectioned,
and the tubular collecting part 1, which is provided in order to collect PM particles,
is provided with a collecting pipe 1-1 constituting a precipitation electrode, having
a predetermined length and having a collecting wall 1-1k, and with a discharge electrode
1-2 charging PM contained in exhaust gas. The collecting pipe 1-1 constituting a precipitation
electrode has an exhaust gas inlet 1-1a at an end on an upstream side (diesel engine
side) thereof, and a low PM concentration exhaust gas outlet pipe 3 and a high PM
concentration exhaust gas outlet portion 1-1b are provided in a communicating manner
in the vicinity of an axial center of an end on a downstream side thereof and in the
vicinity of an inner peripheral face of the end on the downstream side, respectively.
The discharge electrode 1-2 is composed of a main electrode 1-2a extending in the
vicinity of the collecting pipe 1-1 constituting a precipitation electrode and over
a substantially entire length thereof, and a group of electrode needles 1-2b projecting
radially and disposed at desired intervals in a longitudinal direction of the main
electrode 1-2a. In the discharge electrode 1-2 thus configured is supported at both
ends of the main electrode 1-2a by supports 4 hung in a seal air intake pipe portion
1-1c disposed on the exhaust gas inlet 1-1a side of the collecting pipe 1-1 and in
a seal air intake pipe portion 3-1 provided at an inlet of the low-PM-concentration
exhaust gas outlet pipe 3. It should be noted that, though not shown in the figures,
the discharge electrode 1-2 is supported by insulated stays at desired intervals inside
the collecting pipe 1-1, if necessary. In addition, the discharge electrode 1-2 is
wired to high-voltage power supply apparatus (not shown) installed outside, and supplied
with controlled high-voltage power.
[0029] The segregating and collecting part 2 provided on the downstream side of the tubular
collecting part 1 in a flowing direction of the exhaust gas is composed of a cyclone
collecting means 2-1 serving as a segregating means. This cyclone collecting means
2-1 is composed of one tangential cyclone 2-1a connected via a communicating pipe
5-1 to the high-PM-concentration exhaust gas outlet portion 1-1b of the collecting
pipe 1-1, and further a discharge pipe 6-1 for causing purified gas which has passed
through the tangential cyclone 2-1a to mix into low PM concentration of exhaust gas
flowing in the low-PM-concentration exhaust gas outlet pipe 3 is provided between
the tangential cyclone 2-1a and the low-concentration exhaust gas outlet pipe 3. In
addition, the low-PM-concentration exhaust gas outlet pipe 3 is provided with a flow-rate
control damper 7 for regulating the inflow rate and inflow velocity of the high-concentration
exhaust gas to the tangential cyclone 2-1a and the discharge rate of the low-concentration
exhaust gas.
It should be noted that the dashed line in FIG. 1 shows an example of a combination
of a main engine 12 and an auxiliary engine 13 in a marine diesel engine. In the case
of this marine diesel engine, the modes of engine operation include parallel operation
of the main engine 12 and the auxiliary engine 13 and individual operation thereof,
where the load of each engine also significantly varies, and therefore the total flow
rate of exhaust gas significantly varies. In addition, in the case of a large-displacement
engine, a plurality of the collecting pipes 1-1 may be provided in parallel (not shown).
[0030] An exhaust gas treatment equipment for a diesel engine shown as a second embodiment
equipment of the present invention in FIG. 2 has the same configuration as the first
embodiment equipment, except that the cyclone collecting means 2-1 is composed of
two tangential cyclones 2-1a. That is, the cyclone collecting means 2-1 is configured
such that the two tangential cyclones 2-1a are parallel-connected via communicating
pipes 5-1, 5-2 to the high-PM-concentration exhaust gas outlet portion 1-1b of the
collecting pipe 1-1, and, also in this case, discharge pipes 6-1, 6-2 are provided
for causing purified gas which have passed through each of the tangential cyclones
2-1a to mix into the low PM concentration of exhaust gas flowing in the low-PM-concentration
exhaust gas outlet pipe 3.
[0031] In the above exhaust gas treatment equipments for a diesel engine shown in FIGS.
1 and 2, the PM in the exhaust gas flowing into the collecting pipe 1-1 from the exhaust
gas inlet 1-1a is charged by discharge between the collecting wall 1-1k which is an
inner wall of the collecting pipe 1-1 constituting the precipitation electrode and
the discharge electrode 1-2, the charged PM particles are collected on the collecting
wall 1-1k by coulomb force. An exhaust gas stream including PM in high concentration
is created such that PM particles collected from an exhaust gas stream in the vicinity
of the axial center are further deposited on the PM particles collected on the collecting
wall 1-1k of the collecting pipe 1-1 and gradually grown into masses over time, and
the PM masses flow while being concentrated in the vicinity of the collecting wall
by repeating detachment due to the exhaust flow and reattachment to the tubular collecting
wall 1-1k due to the coulomb force involved in the discharge (charge), and, as the
same time, the PM in the exhaust gas flowing in the vicinity of the axial center of
the collecting pipe 1-1 is gradually diluted by collecting the PM on the collecting
wall 1-1k, so that the exhaust gas flows downstream as a stream having only a low
PM concentration. That is, the exhaust gas which has flowed into the collecting pipe
1-1 from the exhaust gas inlet 1-1a is separated into a high PM concentration of exhaust
gas stream and a low PM concentration of exhaust gas stream in the course of flowing
down in the tubular collecting part 1, and the high-PM-concentration exhaust gas stream
flows downstream in the vicinity of the collecting wall 1-1k of the inner wall of
the collecting pipe 1-1, and the low PM concentration of exhaust gas stream in the
vicinity of the axial center of the collecting pipe 1-1. Then, in the case of the
exhaust gas treatment equipment for a diesel engine shown in FIG. 1, in the downstream
side of the collecting pipe 1-1, the high PM concentration of exhaust gas stream which
has flowed in the vicinity of the collecting wall 1-1k of the inner wall of the collecting
pipe 1-1 is introduced into the tangential cyclone 2-1a from the high-PM-concentration
exhaust gas outlet portion 1-1b of the collecting pipe 1-1 via the communicating pipe
5-1 and the PM is separated by centrifugation. While, in the case of the diesel-engine
exhaust gas treatment equipment shown in FIG. 2, the high PM concentration of exhaust
gas stream which has flowed in the vicinity of the collecting wall 1-1k of the inner
wall of the collecting pipe 1-1 is introduced into the two tangential cyclones 2-1a
from the high-PM-concentration exhaust gas outlet portion 1-1b of the collecting pipe
1-1 via the communicating pipes 5-1, 5-2 and the PM is separated by centrifugation.
On the other hand, the low PM concentration of exhaust gas stream flowing in the vicinity
of the axial center portion of the collecting pipe 1-1 is discharged outside through
the low-PM-concentration exhaust gas outlet pipe 3 provided in the vicinity of the
axial center portion of the collecting pipe 1-1, in both the cases of the exhaust
gas treatment equipments for a diesel engine in FIGS. 1 and 2. In addition, the exhaust
gas streams purified by the tangential cyclones 2-1a are caused to mixed into the
low PM concentration of exhaust gas stream flowing in the low-PM-concentration exhaust
gas outlet pipe 3 via the discharge pipes 6-1, 6-1, and 6-2, respectively.
It should be noted that, in the case of the exhaust gas treatment equipment for a
diesel engine shown in FIG. 2 where the cyclone collecting means 2-1 is composed of
the two tangential cyclones 2-1a, the number of tangential cyclones can be determined
according to the flow rate of high PM concentration of exhaust gas exhausted from
the high-concentration exhaust gas outlet portion 1-1b, and the two tangential cyclones
2-1a can be used alternately.
[0032] As described above, in the cases of the exhaust gas treatment equipments for a diesel
engine of the present invention shown in FIGS. 1 and 2, since only high PM concentration
of exhaust gas (part of the entire exhaust gas amount) can be introduced into a cyclone,
PM can be collected/segregated and collected efficiently by a small-sized cyclone.
[0033] Next, an exhaust gas treatment equipment for a diesel engine shown as a third embodiment
equipment in FIG. 3 has the same configuration as the diesel-engine exhaust gas treatment
equipment shown in FIGS. 1 or 2, except that a radially-expanding tubular portion
1-1d having a gradually-increasing diameter and a large-diameter tubular portion 1-1e
communicating with the radially-expanding tubular portion 1-1e are formed at the end
on the downstream side of the collecting pipe 1-1 constituting the precipitation electrode
of the tubular collecting part 1, and that the low-PM-concentration exhaust gas outlet
pipe 3 is provided in a communicating manner in the vicinity of an axial center of
the large-diameter tubular portion 1-1e, and the high-PM-concentration exhaust gas
outlet portion 1-1b in the vicinity of an inner peripheral face thereof. In the case
of the diesel-engine exhaust gas treatment equipment for a diesel engine thus configured,
at the end on the downstream side of the collecting pipe 1-1, the high PM concentration
of exhaust gas stream is gradually slowed down by the radially-expanding tubular portion
1-1d, so that the PM can reliably be introduced into the high-PM-concentration exhaust
gas outlet portion 1-1b provided in a communicating manner in the vicinity of the
inner peripheral face of the large-diameter tubular portion 1-1e. It should be noted
that it is further preferred that the electrode needles 1-2b of the discharge electrode
1-2 be continuously provided to the radially-expanding tubular portion 1-1b at the
end on the downstream side of the collecting pipe 1-1.
[0034] In addition, in the exhaust gas treatment equipment for a diesel engine shown in
FIG. 3, when the collecting pipe 1-1 is disposed vertically downward, as shown in
FIG. 4, a bottom wall face 1-1e' of the large-diameter tubular portion 1-1e is inclined
downward to the communicating pipe 5-1, as shown in FIG. 4. Such means is taken to
make it easy to collect liquid components, such as dropped SOF or sulfate, by causing
the liquid components to flow down to the cyclone side, and to make it easy to collect
oxidized scales (metal-oxide scales or the like) detached from the collecting wall
1-1k when the oxidized scales are generated by corrosion of the collecting wall 1-1k
of the inner face of the collecting pipe 1-1 caused by the PM, sulfate, or the like.
[0035] In addition, an exhaust gas treatment equipment for a diesel engine shown as fourth
embodiment equipment in FIGS. 5 and 6 has the same configuration as the exhaust gas
treatment equipment for a diesel engine shown in FIG. 1 or 2, except that a radially-expanding
tubular portion 1-1d having a gradually-increasing diameter and a large-diameter tubular
portion 1-1e communicating with the radially-expanding tubular portion 1-1e are formed
at the end on the downstream side of the collecting pipe 1-1 constituting the precipitation
electrode of the tubular collecting part 1, that the low-PM-concentration exhaust
gas outlet pipe 3 is provided in a communicating manner in the vicinity of an axial
center of the large-diameter tubular portion 1-1e, and the high-PM-concentration exhaust
gas outlet portion 1-1b in the vicinity of an inner peripheral face thereof, and further
that the discharge electrode 1-2 and the electrode needles 1-2b are extended to the
area of the radially-expanding tubular portion 1-1d and the large-diameter tubular
portion 1-1e communicating with the radially-expanding tubular portion. Incidentally,
the reference numeral 1-2c denotes a support ring supporting each of a plurality of
branches of the discharge electrode 1-2.
In the case of the exhaust gas treatment equipment for a diesel engine thus configured,
in the end on the downstream side of the collecting pipe 1-1, not only is it possible
to collect the PM more effectively since the high PM concentration of exhaust gas
stream is gradually slowed down by the radially-expanding tubular portion 1-1d, but
it is also possible to increase the collection efficiency in the cyclone collecting
means 2-1 further since the PM masses grow even after the PM has flowed into the wide
tubular portion 1-1e, so that the exhaust gas can be further purified.
[0036] Further, an exhaust gas treatment equipment for a diesel engine shown as a fifth
embodiment equipment in FIG. 7 is configured such that an exhaust gas intake chamber
1-1f is disposed upstream from the collecting pipe 1-1, a narrowing portion 1-1f and
a radially-expanding portion 1-1h are disposed between the exhaust gas intake chamber
1-1f and the collecting pipe 1-1, the narrowing portion 1-1g and the radially-expanding
portion 1-1h are also provided with the electrode needles 1-2b, and the exhaust gas
inlet 1-1a to the exhaust gas intake chamber 1-1f and a seal air inlet 1-1j to a seal
air intake chamber 1-1i are disposed so as to face each other.
In the exhaust gas treatment equipment for a diesel engine thus configured, when the
length of the collecting pipe 1-1 is represented by L, and the inner diameter of the
collecting pipe 1-1 is represented by D, it is preferred that the condition of 3D
≤ L ≤ 15D, more preferably, 5D ≤ L ≤ 10D, be satisfied. This is because, if L is less
than 3D, the exhaust gas stream cannot sufficiently be rectified and the disturbance
cannot completely be settled down, so that the increase in the PM concentration on
the collecting wall 1-1k is promoted, and, on the other hand, if L is more than 15D,
there is no difference in the degree of increase in the PM concentration, but the
size of the equipment increases and the spatial efficiency thus deteriorates. In addition,
the reason why the condition of 5D ≤ L ≤ 10D is preferred is because, if L is equal
to or more than 5D, the stream is particularly well rectified and the increase in
the PM concentration in the vicinity of the collecting wall 1-1k becomes stable, and
the difference in the degree of increase in the PM concentration becomes small within
10D and a practical advantageous effect can then be obtained, so that the increase
in the size of the equipment can be suppressed. Additionally, as specific examples
of the dimensions of each part, the length L of the collecting pipe 1-1 is 3 m, the
inner diameter of the collecting pipe 1-1 is ø 400 mm, the length of the narrowing
portion 1-1g is 375 mm, the inner diameter of the narrowing portion 1-1g is ø 220
mm, and the expansion angle θ of the radially-expanding portion 1-1h is 30 degrees.
Further, the exhaust gas which has flowed from the exhaust gas inlet 1-1a into the
exhaust gas intake chamber 1-1f passes through the narrowing portion 1-1g by which
the disturbance of the exhaust gas stream after the radially-expanding portion 1-1h
is suppressed and the gas stream is immediately stabilized and the increase in the
PM concentration on the collecting wall 1-1k of the collecting pipe inner wall and
the dilution in the PM concentration in the vicinity of the collecting pipe axial
center are promoted. Besides, in the narrowing portion 1-1g, since a distance between
the electrodes and the particulates is short, all the particles can reliably be charged
and the particles are attached to the collecting wall 1-1k of the collecting pipe
inner wall and the collection performance can be improved. Here, the reason why the
exhaust gas is caused to flow into the exhaust gas intake chamber 1-1f from the opposite
sides is because, by causing the exhaust gas to flow symmetrically into the collecting
pipe 1-1, the exhaust gas stream flows in a well-balanced manner and the exhaust gas
stream is less disturbed and immediately rectified, so that the exhaust gas stream,
which is also an axially-short stream, can be well-rectified, which is preferred.
In addition, it is also preferred that the seal air to the electrode be caused to
flow into the seal air intake chamber 1-1i from the opposite sides.
[0037] Next, a cyclone collecting means shown in FIG. 8 is composed of a plurality of tangential
cyclones having different treatment capacities, for example, the following three types
of cyclones: a low-treatment-capacity tangential cyclone 2-1b; an intermediate-treatment-capacity
tangential cyclone 2-1c; and a high-treatment-capacity tangential cyclone 2-1d, and
the cyclone collecting means is configured such that the respective tangential cyclones
2-1b, 2-1c, 2-1d are connected via communicating pipes 8-1, 8-2, 8-3 connected radially
to the high-PM-concentration exhaust gas outlet portion 1-1b of the collecting pipe1-1,
and flow-rate control dampers 9-1, 9-2, 9-3 are provided at the respective high-PM-concentration
exhaust gas inlets of the communicating pipes 8-1, 8-2, 8-3.
When the cyclone collecting means is thus composed of tangential cyclones having different
treatment capacities, not only does it become possible to select more appropriately
each tangential cyclone according to the exhaust gas flow rate that changes according
to a change in operating conditions or the engine load ratio involved in the parallel
operation or individual operation of the main engine and the auxiliary engine in a
marine engine, but it also becomes possible to control more appropriately the tangential
velocity of exhaust gas flowing in each tangential cyclone by controlling the respective
flow-rate control dampers 9-1, 9-2, 9-3 provided for the tangential cyclones in combination
with the damper provided in the low-PM-concentration exhaust gas outlet pipe 3, so
that a high collection efficiency can be ensured and maintained over a wide range
of engine load ratios, or the like.
[0038] In addition, as shown in FIGS. 9(a) and 9(b), when the discharge pipe 6-1 provided
to cause the purified gas which has passed through the tangential cyclone to mix into
the low PM concentration of exhaust gas is provided with an air nozzle 10 or a fan
11 driven by a motor 11-1 for accelerating and sucking the purified gas which has
passed through the tangential cyclone, the purified gas stream which has passed through
the tangential cyclone is given kinetic energy and then accelerated and sucked, and
the pressure loss in the exhaust gas purification equipment is improved so as to be
lower, so that the fuel economy can be improved.
[0039] Further, FIGS. 10 and 11 each illustrate the case where the tubular collecting part
1 in the present invention equipment, for example, the tubular collecting part 1 having
the radially-expanding portion 1-1e at the end on the downstream side of the collecting
pipe 1-1, is disposed substantially vertically to an engine room floor surface, FIG.
10 showing an example of disposing the tubular collecting part 1 substantially vertically
and downward, and FIG. 11 showing an example of disposing the tubular collecting part
1 substantially vertically and upward. Here, in the case where the tubular collecting
part 1 is disposed substantially vertically and downward, as shown in FIG. 10, there
is a space-saving advantage since the tubular collecting part 1 can double as a pipe
of an exhaust pipe to a funnel (not shown). On the other hand, in the case where the
tubular collecting part 1 is disposed substantially vertically and upward, as shown
in FIG. 11, there is not only the advantage that it becomes easy to collect the falling
PM, but also the advantage that, when SOF, sulfate, or the like, attached to the collecting
wall face is liquefied, it becomes easy to collect the liquefied components because
of falling down the surface of the collecting wall, and further the advantage it becomes
easy to collect even heavy oxidized scales corroded by sulfate or the like detaching
and falling from the surface of the wall. Besides, in a case where the tubular collecting
part 1 is disposed substantially horizontally, there is the advantage that workability
at a maintenance time of the collecting pipe, the discharge electrode, and the like
becomes excellent since the tubular collecting part 1 is maintained at a horizontally
substantially constant height from the floor surface of the engine room in which the
engine is placed.
Industrial Applicability
[0040] Since the exhaust gas purification equipment for a diesel engine according to the
present invention has a system in which the exhaust gas is purified by introducing
a stream of part of the entire exhaust gas amount which has been concentrated up to
a high PM concentration by condensing PM in advance into the cyclone and thereby the
size of the cyclone can be reduced, and besides, when the system is such that the
cyclone collecting means is composed of a plurality of tangential cyclones so that
the high PM concentration of exhaust gas stream discharged through the high-PM-concentration
exhaust gas outlet portion is selectively introduced into the tangential cyclones
according to the flow rate of the exhaust gas, it becomes possible to select an appropriate
treatment capacity and the appropriate number of the tangential cyclones in a well-balanced
manner according to a significant increase or decrease in the exhaust gas flow rate
(flow velocity) involved in a change in operating conditions or a fluctuation in engine
load ratio caused by parallel operation or individual operation of the main engine
and the auxiliary engine in a marine engine, in addition to the function effect of
the tangential cyclone having a better collection capacity than an axial cyclone,
so that a high PM collection efficiency can be ensured and maintained by responding
to every change in the exhaust gas flow rate. In addition, since the tangential velocity
of the exhaust gas flowing into the tangential cyclone can be appropriately controlled
by controlling the opening position of the damper provided in the low-PM-concentration
exhaust gas outlet pipe, a high PM collection efficiency can be ensured and maintained
and such a problem as a deterioration in fuel economy due to an excessive pressure
loss in the exhaust gas purification equipment can be solved. Achieving many advantageous
effects such as these, the diesel-engine exhaust gas purification equipment according
to the present invention makes a great consideration to exhaust gas purification treatment
for a diesel engine for various applications, such as for watercrafts, for automobiles,
or for industrial purposes, using a low-grade fuel equal to or less than fuel oil.
Reference Signs List
[0041]
- 1
- tubular collecting part,
- 1-1
- collecting pipe,
- 1-1a
- exhaust gas inlet,
- 1-1b
- high-PM-concentration exhaust gas outlet portion,
- 1-1c
- seal air intake pipe portion,
- 1-1d
- radially-expanding tubular portion,
- 1-1e
- large-diameter tubular portion,
- 1-1f
- exhaust gas intake chamber,
- 1-1g
- narrowing portion,
- 1-1h
- radially-expanding portion,
- 1-1i
- seal air intake chamber,
- 1-1j
- seal air inlet,
- 1-1k
- collecting wall,
- 1-2
- discharge electrode,
- 1-2a
- main electrode,
- 1-2b
- electrode needle,
- 1-2c
- support ring,
- 2
- segregating and collecting part,
- 2-1
- cyclone collecting means,
- 2-1a
- tangential cyclone,
- 2-1b
- low-treatment-capacity tangential cyclone,
- 2-1c
- intermediate-treatment-capacity tangential cyclone,
- 2-1d
- high-treatment-capacity tangential cyclone,
- 3
- low-PM-concentration exhaust gas outlet pipe,
- 3-1
- seal air intake pipe portion,
- 4
- support,
- 5-1
- communicating pipe,
- 5-2
- communicating pipe,
- 8-1
- communicating pipe,
- 8-2
- communicating pipe,
- 8-3
- communicating pipe,
- 6-1
- discharged pipe
- 6-2
- discharge pipe,
- 7
- flow-rate control damper,
- 9-1
- flow-rate control damper,
- 9-2
- flow-rate control damper,
- 9-3
- flow-rate control damper,
- 10
- air nozzle,
- 11
- fan,
- 11-1
- motor,
- 12
- main engine,
- 13
- auxiliary engine.