CN100404808C - Exhaust gas cleaner for engine - Google Patents
Exhaust gas cleaner for engine Download PDFInfo
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- CN100404808C CN100404808C CNB2004800286338A CN200480028633A CN100404808C CN 100404808 C CN100404808 C CN 100404808C CN B2004800286338 A CNB2004800286338 A CN B2004800286338A CN 200480028633 A CN200480028633 A CN 200480028633A CN 100404808 C CN100404808 C CN 100404808C
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- reducing agent
- nozzle
- temperature
- exhaust
- exhaust gas
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- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 161
- 239000003054 catalyst Substances 0.000 claims abstract description 28
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 21
- 238000001514 detection method Methods 0.000 claims abstract description 17
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims description 91
- 239000007789 gas Substances 0.000 claims description 79
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 37
- 239000004202 carbamide Substances 0.000 claims description 37
- 239000007864 aqueous solution Substances 0.000 claims description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 11
- 238000002347 injection Methods 0.000 abstract description 9
- 239000007924 injection Substances 0.000 abstract description 9
- 238000001816 cooling Methods 0.000 abstract description 8
- 210000002700 urine Anatomy 0.000 abstract 4
- 238000004140 cleaning Methods 0.000 abstract 2
- WTHDKMILWLGDKL-UHFFFAOYSA-N urea;hydrate Chemical compound O.NC(N)=O WTHDKMILWLGDKL-UHFFFAOYSA-N 0.000 description 81
- GQPLMRYTRLFLPF-UHFFFAOYSA-N Nitrous Oxide Chemical compound [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 description 62
- 239000007921 spray Substances 0.000 description 40
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 24
- 239000007787 solid Substances 0.000 description 17
- 230000009471 action Effects 0.000 description 13
- 229910021529 ammonia Inorganic materials 0.000 description 12
- 230000015572 biosynthetic process Effects 0.000 description 9
- 239000001272 nitrous oxide Substances 0.000 description 9
- 238000003825 pressing Methods 0.000 description 8
- 238000006722 reduction reaction Methods 0.000 description 7
- 238000000354 decomposition reaction Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 230000009467 reduction Effects 0.000 description 4
- 238000002425 crystallisation Methods 0.000 description 3
- 230000008025 crystallization Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000009692 water atomization Methods 0.000 description 3
- 239000013078 crystal Substances 0.000 description 2
- 230000008030 elimination Effects 0.000 description 2
- 238000003379 elimination reaction Methods 0.000 description 2
- 229910002060 Fe-Cr-Al alloy Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000001413 cellular effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- KEUKAQNPUBYCIC-UHFFFAOYSA-N ethaneperoxoic acid;hydrogen peroxide Chemical compound OO.CC(=O)OO KEUKAQNPUBYCIC-UHFFFAOYSA-N 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 230000003434 inspiratory effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/40—Engine management systems
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- Exhaust Gas After Treatment (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
An exhaust gas cleaner of an engine in which cleaning efficiency of Nox is enhanced by preventing clogging of an injection nozzle for supplying a reducing agent to the upstream side of exhaust gas of a reducing catalyst. Using a detection signal S1 of the exhaust gas temperature from an exhaust gas temperature sensor (9), a reducing agent supply unit (6) sets a supply quantity larger than a lower limit of the supply quantity for cooling the inside of an injection nozzle (5) at a temperature below the crystallizing point of urine water and supplies the set supply quantity of urine water to the injection nozzle (5) at the detected exhaust gas temperature. Consequently, the inside of the injection nozzle (5) is cooled at a temperature below the crystallizing point of urine water. Since urine water is not crystallizing in the injection nozzle (5), the injection nozzle (5) can be prevented from clogging and the cleaning efficiency of Nox can be enhanced.
Description
Technical field
The present invention relates to the Exhaust gas purifying device of the nitrogen oxide (NOx) that a kind of diesel engine that uses reducing agent reduction to remove and carry from moving vehicle, petrol engine etc. discharge, particularly relate to prevent to the exhaust-gas upstream side of reducing catalyst supply with reducing agent nozzle obstruction and when this nozzle takes place to stop up, eliminate its obstruction and improve the Exhaust gas purifying device of motor of the purified treatment efficient of NOx.
Background technique
Come the system of purifying exhaust gas as the particularly NOx in the fine particle material of removing from the exhaust that motor is discharged (PM), propose to have several Exhaust gas purifying devices.This Exhaust gas purifying device is such device: in engine's exhaust system reducing catalyst is set, in the exhaust passageway of the upstream side of this reducing catalyst, spray and supply with reducing agent, thereby making NOx and reducing agent in the exhaust produce the catalyst reduction reaction, is harmless composition with the NOx purified treatment.Reducing agent is stored in the storage tank with liquid condition at normal temperatures, supplies with the reducing agent of requirement from nozzle ejection.Reduction reaction be to use with the reactive good ammonia of NOx as reducing agent, use the aqueous solution of urea that adds water decomposition and just be easy to generate ammonia, ammonia spirit, other the reducing agent aqueous solution (for example with reference to TOHKEMY 2000-27627 communique).
But, in above-mentioned Exhaust gas purifying device in the past, control the delivery volume of reducing agent corresponding to the operating condition (delivery temperature or NOx discharge capacity etc.) of motor, but, have and cause the spray orifice that is arranged at the nozzle in the exhaust passageway or arrive the blocked path at this place and can not fully supply with the situation of reducing agent according to the operating condition of motor.Its result might can not successfully carry out in the reduction reaction of the NOx on the above-mentioned reducing catalyst, and NOx is discharged from.
The main cause of the obstruction of said nozzle is, as the urea in the aqueous solution of urea (hereinafter referred to as " urea water ") of reducing agent, at spray orifice or arrive the path intercrystallineization of this spray orifice and solidify (hereinafter referred to as " solid urea ").This be because, because urea water condenses at 100 ℃, so urea crystals takes place when urea water is heated to more than 100 ℃ or 100 ℃.At this, in the injection of the common urea water of being undertaken by nozzle is supplied with, the urea water of supplying with from storage tank is (when supplying with compressed-air actuated reducing agent supply system when being that nozzle is supplied with urea water, be urea water and pressurized air) cooling jet inside, even this nozzle is by the exhaust heating from motor, its urea water is also less than 100 ℃.But the delivery volume of urea water reduces, and when cooling jet was inner fully, the urea water of nozzle interior reached more than 100 ℃ or 100 ℃, generation urea crystals and might cause obstruction.
In addition, because the fusing point of solid urea is 132 ℃,, increase promptly fusible above-mentioned solid urea, the obstruction of elimination nozzle so owing to the exhaust from motor, nozzle delivery temperature nearby rises to the input of this nozzle is hot.
But, the reducing agent feed mechanism supplies with pressurized air when nozzle is supplied with urea water, when making the so-called pneumatic type reducing agent supply part that sprays after this urea water atomizing, then owing to supply to the pressurized air cooling jet inside of nozzle at ordinary times, so the temperature of nozzle interior can not go up more than 132 ℃ or 132 ℃, hinder the fusing of solid urea.Therefore, may adhere to crystallization in said nozzle inside and cakey solid urea causes the obstruction of nozzle.In addition, in this case,, make the solid urea fusing, consider to improve the delivery temperature in the exhaust passageway, but be not very wise move for motor like this in order to improve the temperature of nozzle interior.
Summary of the invention
Therefore, The present invention be directed to the problems referred to above point and make, purpose is to provide a kind of preventing to supply with the spray nozzle clogging of reducing agent and eliminate the Exhaust gas purifying device of the motor of its purified treatment efficient of stopping up, improving NOx when this spray nozzle clogging takes place to the exhaust-gas upstream side of reducing catalyst.
The Exhaust gas purifying device of the motor described in the technological scheme 1 comprises: reducing catalyst, and it is equipped in the engine exhaust system, is used for reducing the nitrogen oxide of purifying exhaust gas with reducing agent; The reducing agent supply part, it has nozzle, and this nozzle is supplied with reducing agent and pressurized air simultaneously, makes this reducing agent atomizing back exhaust-gas upstream side to above-mentioned reducing catalyst in the exhaust passageway of above-mentioned vent systems spray supply; Temperature detection part, it is located near the exhaust-gas upstream side of said nozzle, is used to detect the delivery temperature in the exhaust passageway; Wherein, above-mentioned reducing agent supply part, be used to testing signal from the delivery temperature of said temperature detection part, this reducing agent delivery volume is set under its delivery temperature, said nozzle inside is cooled to be lower than the reducing agent crystallized temperature delivery volume lower limit or more than the lower limit, supply with reducing agent with this reducing agent delivery volume to this nozzle.
According to such formation, be used to testing signal from the delivery temperature of temperature detection part, the reducing agent supply part, this reducing agent delivery volume is set under above-mentioned detected delivery temperature, said nozzle inside is cooled to be lower than the reducing agent crystallized temperature delivery volume lower limit or more than the lower limit, supply with reducing agent with the delivery volume of its setting to nozzle.By the supply of such reducing agent, nozzle interior is cooled to below the reducing agent crystallized temperature.
In the Exhaust gas purifying device of technological scheme 2 described motors, above-mentioned reducing agent supply part has such control circuit, its input is from the testing signal of the delivery temperature of said temperature detection part, and the signal of the operating condition of input motor, obtain the delivery volume of the reducing agent under this engine operating status, and obtain under its delivery temperature, said nozzle inside be cooled to be lower than the lower limit of delivery volume of the reducing agent of reducing agent crystallized temperature, relatively the two sets the reducing agent delivery volume.Thus, the control circuit that is had with the reducing agent supply part, input is from the testing signal of the delivery temperature of said temperature detection part, and import the signal of the operating condition of motor at that time, obtain the delivery volume of the reducing agent under the engine operating status at this moment, and obtain under above-mentioned detected delivery temperature, said nozzle inside be cooled to be lower than the lower limit of delivery volume of the reducing agent of reducing agent crystallized temperature, relatively the two sets the delivery volume of reducing agent.
In the Exhaust gas purifying device of technological scheme 3 described motors, above-mentioned reducing agent is an aqueous solution of urea.Thus, will add water decomposition and the aqueous solution of urea that is easy to generate ammonia as reducing agent, reduce nitrogen oxide in the purifying exhaust gas.
In addition, the Exhaust gas purifying device of technological scheme 4 described motors comprises: reducing catalyst, and it is equipped in the engine exhaust system, is used for reducing the nitrogen oxide of purifying exhaust gas with reducing agent; The reducing agent supply part, it has nozzle, and this nozzle is supplied with reducing agent and pressurized air simultaneously, makes this reducing agent atomizing back exhaust-gas upstream side to above-mentioned reducing catalyst in the exhaust passageway of above-mentioned vent systems spray supply; Temperature detection part, it is located near the exhaust-gas upstream side of said nozzle, is used to detect the delivery temperature in the exhaust passageway; Wherein, above-mentioned reducing agent supply part has the pressure-detecting device of the internal pressure that is used to detect said nozzle, utilize the testing signal of the internal pressure of this nozzle, when its pressure is that specified value or specified value stop when above supplying with pressurized air and reducing agent to nozzle, be used to testing signal, when nozzle delivery temperature nearby is that the fusing point of reducing agent or fusing point begin to supply with pressurized air and reducing agent to nozzle when above again from the delivery temperature of said temperature detection part.
According to such formation, the reducing agent supply part utilizes the testing signal by the detected nozzle interior pressure of pressure-detecting device, when above-mentioned detected pressure is that specified value or specified value stop when above supplying with pressurized air and reducing agent to nozzle, be used to testing signal, when nozzle delivery temperature nearby is that the fusing point of reducing agent or fusing point begin to supply with pressurized air and reducing agent to nozzle when above again from the delivery temperature of said temperature detection part.Thus, suppress the cooling of nozzle interior, eliminate the obstruction of nozzle by the delivery temperature in the exhaust passageway.
In the Exhaust gas purifying device of technological scheme 5 described motors, above-mentioned reducing agent supply part has control circuit, this control circuit is controlled, feasible input is from the testing signal of the nozzle interior pressure of above-mentioned pressure-detecting device, and input is from the testing signal of the delivery temperature of said temperature detection part, when nozzle interior pressure is that specified value or specified value stop when above supplying with pressurized air and reducing agent to nozzle, when nozzle delivery temperature nearby is that the fusing point of reducing agent or fusing point begin to supply with pressurized air and reducing agent to nozzle when above again.Thus, control with the control circuit that the reducing agent supply part is had, feasible input is from the testing signal of the nozzle interior pressure of pressure-detecting device, and input is from the testing signal of the delivery temperature of said temperature detection part, when nozzle interior pressure is that specified value or specified value stop when above supplying with pressurized air and reducing agent to nozzle, when nozzle delivery temperature nearby is that the fusing point of reducing agent or fusing point begin to supply with pressurized air and reducing agent to nozzle when above again.
In the Exhaust gas purifying device of technological scheme 6 described motors, above-mentioned reducing agent is an aqueous solution of urea.Thus, will add water decomposition and the aqueous solution of urea that is easy to generate ammonia as reducing agent, reduce nitrogen oxide in the purifying exhaust gas.
In the Exhaust gas purifying device of technological scheme 7 described motors, the nozzle delivery temperature nearby that begins again when said nozzle is supplied with pressurized air and reducing agent is more than 132 ℃ or 132 ℃.Thus, nozzle interior can be heated to the fusing point of the urea in the aqueous solution of urea or the temperature more than the fusing point.
Exhaust gas purifying device according to technological scheme 1 described motor, be set under detected delivery temperature, nozzle interior be cooled to be lower than the lower limit of delivery volume of reducing agent crystallized temperature or the reducing agent more than the lower limit by supply, nozzle interior is cooled and reducing agent is non-crystallizable, can prevent this spray nozzle clogging.Therefore, can improve the purified treatment efficient of NOx.
In addition, Exhaust gas purifying device according to technological scheme 2 described motors, the delivery volume of the reducing agent under the engine operating status and under detected delivery temperature more at that time, nozzle interior is cooled to be lower than the lower limit of delivery volume of the reducing agent of reducing agent crystallized temperature, can often be set at the reducing agent under delivery temperature at that time delivery volume lower limit or more than the lower limit, supply with reducing agent.Therefore, nozzle interior is cooled and reducing agent is non-crystallizable, can prevent this spray nozzle clogging.
In addition, according to the Exhaust gas purifying device of technological scheme 3 described motors, directly do not use ammonia as reducing agent, and add the aqueous solution of urea that water decomposition just is easy to generate ammonia by use, NOx in the exhaust is converted into harmless composition, can improves the purified treatment efficient of NOx.
In addition, Exhaust gas purifying device according to technological scheme 4 described motors, judging when having caused spray nozzle clogging, stop to supply with pressurized air and reducing agent to this nozzle, suppress the cooling of nozzle interior, under this state, when judging heating by the exhaust in the exhaust passageway reducing agent of nozzle interior having been melted, can begin again to supply with pressurized air and reducing agent to this nozzle.Thus, when spray nozzle clogging takes place,, also can eliminate its obstruction even the delivery temperature in the exhaust passageway is low.Therefore, can improve the purified treatment efficient of NOx.
In addition, Exhaust gas purifying device according to technological scheme 5 described motors, the control circuit that is had by the reducing agent supply part, can carry out following control, when the internal pressure of nozzle is that specified value or specified value are when above, be judged as and caused spray nozzle clogging, stop to supply with pressurized air and reducing agent to nozzle, when nozzle delivery temperature nearby is that the fusing point of reducing agent or fusing point are when above, be judged as by the heating of its exhaust the reducing agent of nozzle interior has been melted, then begin again to supply with pressurized air and reducing agent to nozzle.Thus, when spray nozzle clogging has taken place,, also can eliminate it and stop up, can improve the purified treatment efficient of NOx even the delivery temperature in the exhaust passageway is low.
In addition, according to the Exhaust gas purifying device of technological scheme 6 described motors, directly do not use ammonia as reducing agent, and add the aqueous solution of urea that water decomposition just is easy to generate ammonia by use, NOx in the exhaust is converted into harmless composition, can improves the purified treatment efficient of NOx.
In addition,, can be used to that exhaust from motor is heated to the fusing point of urea with nozzle interior or more than the fusing point, can make the solid urea fusing of nozzle interior and eliminate the obstruction of this nozzle interior according to the Exhaust gas purifying device of technological scheme 7 described motors.Thus, can improve the purified treatment efficient of NOx.
Description of drawings
Fig. 1 is the concept map of mode of execution of the Exhaust gas purifying device of expression motor of the present invention.
Fig. 2 is reducing agent supply part and the formation of nozzle and the synoptic diagram of action that is used to illustrate the Exhaust gas purifying device of the 1st mode of execution.
Fig. 3 is the flow chart that is used to illustrate the action of above-mentioned Exhaust gas purifying device.
Fig. 4 is reducing agent supply part and the formation of nozzle and the synoptic diagram of action that is used to illustrate the Exhaust gas purifying device of the 2nd mode of execution.
Fig. 5 is the flow chart that is used to illustrate the action of above-mentioned Exhaust gas purifying device.
Description of reference numerals
1: motor
3: reducing catalyst
4: outlet pipe
5: nozzle
6: the reducing agent supply part
7: storage tank
8: supplying tubing
9: exhaust gas temperature sensor
11: the supply valve of urea water
13: the air supply valve
14: the reducing agent supply control circuit
15: engine control circuit
16: pressure transducer
17: shared pipe arrangement
Embodiment
Below, present invention will be described in detail with reference to the accompanying.Fig. 1 is the figure of mode of execution of the Exhaust gas purifying device of expression motor of the present invention.This Exhaust gas purifying device is the NOx that the diesel engine that is used to use the reducing agent reduction to remove to carry from moving vehicle, petrol engine etc. are discharged.With gasoline or diesel oil is the exhaust of the motor 1 of fuel, is discharged to the atmosphere through being equipped with the outlet pipe 4 of NOx reducing catalyst 3 from gas exhaust manifold 2.In detail, in outlet pipe 4 as exhaust passageway, be equipped with nitrous oxide (NO) oxidation catalyst, NOx reducing catalyst, these three kinds of catalyzer of ammoxidation catalyst successively from exhaust-gas upstream side, before and after it, be equipped with temperature transducer, NOx sensor etc., constitute vent systems, but trickle part and not shown.
Above-mentioned NOx reducing catalyst 3 is owing to be that reduction purifies by the NOx's in the exhaust in the outlet pipe 4 by reducing agent, so it has carried for example active component of zeolites on refractory steel integrated type that constitute, that have cellular cross section (monolith) the catalyst carrier body by the steinheilite of pottery or Fe-Cr-Al class.And the active component that is carried on above-mentioned catalyst carrier body is accepted the supply of reducing agent and activate, effectively NOx is purified to be innoxious substance.
In the inside of above-mentioned outlet pipe 4, be equipped with nozzle 5 in the exhaust-gas upstream side of NOx reducing catalyst 3.This nozzle 5 is supplied with reducing agent to the exhaust-gas upstream side of above-mentioned NOx reducing catalyst 3, so by reducing agent supply part 6, together supply with pressurized air with reducing agent, this reducing agent is atomized spray supply.Such device is called as pneumatic type.At this, in outlet pipe 4, set nozzle 5 towards the downstream side or set nozzle 5 with becoming oblique shape with suitable angle tilt with flow direction of exhaust gases A almost parallel ground.In addition, reducing agent supply part 6 is supplied to the reducing agent that is stored in the storage tank 7 by supplying tubing 8.And, constitute reducing agent supply part from reducing agent to the exhaust-gas upstream side of the reducing agent catalyzer 3 of NOx that supply with by said nozzle 5 and reducing agent supply part 6.
In the present embodiment, use is sprayed the aqueous solution of urea (urea water) of supply as reducing agent by said nozzle 5.Also can use other ammonia spirit etc.And, spray the urea water of supplying with nozzle 5, add water decomposition by the exhaust heat in the outlet pipe 4 and be easy to generate ammonia.The ammonia that obtains in the reducing catalyst 3 of NOx with exhaust in NOx reaction, be cleaned into water and innocuous gas.Urea water is the aqueous solution of the urea of solid or body of powder, lodges in the storage tank 7, is fed into reducing agent supply part 6 by supplying tubing 8.
In the inside of above-mentioned outlet pipe 4, nearby be provided with exhaust gas temperature sensor 9 in the exhaust-gas upstream side of nozzle 5.This exhaust gas temperature sensor 9 is as the temperature detection part that is used to detect the delivery temperature in the outlet pipe 4, in the present embodiment, detects the exhaust-gas upstream side delivery temperature nearby of said nozzle 5.And, be transferred into above-mentioned reducing agent supply part 6 with these exhaust gas temperature sensor 9 detected delivery temperature testing signals.
Fig. 2 is reducing agent supply part 6 and the formation of nozzle 5 and the synoptic diagram of action that is used to illustrate the Exhaust gas purifying device of the 1st mode of execution.This reducing agent supply part 6 constitutes like this: be used to the testing signal from the delivery temperature of above-mentioned exhaust gas temperature sensor 9, be set under its delivery temperature, said nozzle 5 inside be cooled to be lower than the urea water crystallized temperature delivery volume lower limit or more than the lower limit, supply with urea water to this nozzle 5.That is, as shown in Figure 2, this reducing agent supply part 6 has: be located at from the supplying tubing 8 of storage tank shown in Figure 17 midway, booster pump 10 that the pressure of urea water is risen; Be located at the downstream side of this booster pump 10, the path connection that makes urea water, the supply valve 11 that disconnects; Be located at from the air supplying tubing 12 of omitting illustrated source of compressed air midway, the air supply valve 13 that makes compressed-air actuated path connect, disconnect; Reducing agent supply control circuit 14.
And, above-mentioned reducing agent supply control circuit 14, input is from the testing signal S of the delivery temperature of above-mentioned exhaust gas temperature sensor 9
1, and input is from the signal S of the operating condition of the motor 1 of engine control circuit 15
2Obtain the delivery volume of the urea water under this engine operating status, and obtain under this delivery temperature, said nozzle 5 inside be cooled to be lower than the lower limit of delivery volume of the urea water of urea water crystallized temperature, relatively the two sets the delivery volume of urea water, this reducing agent supply control circuit 14 for example is made of with microcomputer (MPU) control, delivery volume according to the urea water of its setting, transmit control signal to above-mentioned booster pump 10, supply valve 11 and air supply valve 13, control urea water and compressed-air actuated delivery volume nozzle 5.
In addition, above-mentioned engine control circuit 15, input is from the temperature transducer of the delivery temperature (engine exhaust temperature) that detects gas exhaust manifold 2 shown in Figure 1 or omit the testing signal of illustrated NOx sensor, inspiratory flow sensor, speed probe and load sensor etc., control the operating condition of motor 1, this engine control circuit 15 for example is made of with microcomputer (MPU) control, sends the operating condition signal S of the motor 1 of engine exhaust temperature and NOx discharge capacity etc. to above-mentioned reducing agent supply control circuit 14
2
The action of Exhaust gas purifying device of the 1st mode of execution of formation like this is described with reference to Fig. 2 and Fig. 3 then.At first, in Fig. 1, the exhaust that is produced by the running of motor 1,, is discharged to the atmosphere from the end exhaust port of outlet pipe 4 by being equipped on the reducing catalyst 3 of the NOx midway in this outlet pipe 4 through outlet pipes 4 from gas exhaust manifold 2.At this moment, in the inside of above-mentioned outlet pipe 4, spray urea water from the nozzle 5 of the exhaust-gas upstream side of the reducing catalyst 3 that is equipped on NOx.After from the storage tank 7 of urea water urea water being supplied to reducing agent supply part 6 by supplying tubing 8, action by this reducing agent supply part 6, supply with the compressed-air actuated urea water of supplying with simultaneously to this nozzle 5, this nozzle 5 sprays supply after making the urea water atomizing.
Under this state, in Fig. 2, by the delivery temperature in the exhaust-gas upstream side of the being located at said nozzle 5 exhaust gas temperature sensor 9 detection outlet pipes 4 nearby, with this testing signal S
1Reducing agent supply control circuit 14 to reducing agent supply part 6 is sent.In addition, from the signal S of the operating condition of motors 1 such as the engine exhaust temperature of engine control circuit 15 and NOx discharge capacity
2Send to reducing agent supply control circuit 14 equally.
So reducing agent supply control circuit 14 utilizes the signal S of the operating condition of the motor of importing 1
2, obtain delivery volume V by the definite urea water (reducing agent) of engine operating status
1(the step S1 of Fig. 3).In addition, above-mentioned reducing agent supply control circuit 14 utilizes the testing signal S of the delivery temperature in the outlet pipe of importing 4
1, obtain lower limit V by the delivery volume of the urea water (reducing agent) that determine, that be cooled to be lower than the urea water crystallized temperature of the delivery temperature near the exhaust-gas upstream side of nozzle 5
2(step S2).And, the delivery volume V of the more above-mentioned urea water of obtaining
1Lower limit V with its delivery volume
2, judge V
1Whether than V
2Little (step S3).
At this moment, judge V
1With V
2Equate or V
1Greater than V
2The time, step S3 enters " NO " side, returns step S1, circulation step S1 → S2 → S3.At this moment, the delivery volume V of the urea water determined of the engine operating status of carving thus
1Lower limit V more than or equal to the delivery volume that nozzle 5 inside is cooled to be lower than the urea water crystallized temperature
2So, with the urea water delivery volume V of present setting
1, the inside that can cool off said nozzle 5.Therefore, reducing agent supply control circuit 14 is kept the aperture of the supply valve 11 and the compressed-air actuated air supply valve 13 of present urea water, and reducing agent supply part 6 is with the delivery volume V of such urea water
1Supply with urea water to nozzle 5.
Then, when judging V
1Less than V
2The time, step S3 enters " YES " side, enters step S4.At this moment, the delivery volume V of the urea water determined of the engine operating status of carving thus
1, be lower than the lower limit V that nozzle 5 inside is cooled to be lower than the delivery volume of urea water crystallized temperature
2So, with the urea water delivery volume V of present setting
1, the inside that can not cool off said nozzle 5.Therefore, reducing agent supply control circuit 14 changes to the supply valve 11 that increases present urea water and aperture one side of compressed-air actuated air supply valve 13, and reducing agent supply part 6 is the lower limit V that is cooled to be lower than the delivery volume of this urea water crystallized temperature for the delivery volume of setting urea water with setting changing
2Or lower limit V
2More than (step S4), supply with urea water to nozzle 5.Thus, with the delivery volume of urea water that change to set at step S4, inside that can cooling jet 5 can prevent that it from stopping up, and improves the purified treatment efficient of NOx.
Then, the running by motor 1 stops, and by the action of reducing agent supply part 6, at first blocks from storage tank 7 and supplies with urea water when nozzle 5 sprays urea water will finishing, and only supplies with pressurized air to nozzle 5 for the time being thereafter.Thus, blow out urea water, finish the injection of urea water from the spray orifice of nozzle 5 or the path that arrives this spray orifice.Like this,, can not be created in residual or so-called " the back drip " of the urea water when nozzle 5 stopped to supply with urea water, can prevent at spray orifice or arrive urea water crystallization in the path of this spray orifice and cause obstruction by going out urea water clearly from nozzle 5.
Fig. 4 is reducing agent supply part 6 and the formation of nozzle 5 and the synoptic diagram of action that is used to illustrate the Exhaust gas purifying device of the 2nd mode of execution.This reducing agent supply part 6, except having above-mentioned formation shown in Figure 2, the pressure transducer 16 that also has the internal pressure that is used to detect said nozzle 5, utilize the testing signal of the internal pressure of this nozzle 5, when its pressure is that specified value or specified value are when above, stop to supply with pressurized air and reducing agent to nozzle 5, be used to testing signal from the delivery temperature of above-mentioned exhaust gas temperature sensor 9, when nozzle 5 delivery temperature nearby is the fusing point of reducing agent or fusing point when above, begin again to supply with pressurized air and reducing agents to nozzle 5.
Above-mentioned pressure transducer 16, pressure-detecting device as the internal pressure that detects said nozzle 5, for example be located at supply with pressurized air and shared pipe arrangement 17 from urea water to nozzle 5 midway, detect the internal pressure of this shared pipe arrangement 17, as the internal pressure of nozzle 5.
And above-mentioned reducing agent supply part 6 utilizes the testing signal S by the internal pressure of above-mentioned pressure transducer 16 detected nozzles 5
3, when its pressure is specified value or specified value when above, stop to supply with pressurized air and urea water to nozzle 5, be used to testing signal S from the delivery temperature of above-mentioned exhaust gas temperature sensor 9
1,, begin again to nozzle 5 supply pressurized air and reducing agents when nozzle 5 delivery temperature nearby is the fusing point (132 ℃) of solid urea or fusing point when above.
In addition, above-mentioned reducing agent supply control circuit 14 is controlled like this: input is from the testing signal S of the internal pressure of the nozzle 5 of above-mentioned pressure transducer 16
3, and input is from the testing signal S of the delivery temperature of above-mentioned exhaust gas temperature sensor 9
1When the internal pressure of nozzle 5 is that specified value or specified value are when above, stop to supply with pressurized air and urea water to nozzle 5, when nozzle 5 delivery temperature nearby is that the fusing point (132 ℃) of solid urea or fusing point are when above, begin again to supply with pressurized air and reducing agent to nozzle 5, this reducing agent supply control circuit 14 for example is made of with microcomputer (MPU) control, according to its controlled supply constantly, to above-mentioned booster pump 10, supply valve 11 and air supply valve 13 are sent control signal, and urea water and the compressed-air actuated supply controlled nozzle 5 stop and beginning supplying with.
The action of Exhaust gas purifying device of the 2nd mode of execution of formation like this is described with reference to Fig. 4 and Fig. 5 then.At first, in Fig. 1, the exhaust that is produced by the running of motor 1,, is discharged to the atmosphere from the end exhaust port of outlet pipe 4 by being equipped on the reducing catalyst 3 of the NOx midway in this outlet pipe 4 through outlet pipes 4 from gas exhaust manifold 2.At this moment, in the inside of above-mentioned outlet pipe 4, spray urea water from the nozzle 5 of the exhaust-gas upstream side of the reducing catalyst 3 that is equipped on NOx.After from the storage tank 7 of urea water urea water being supplied to reducing agent supply part 6 by supplying tubing 8, by the action of this reducing agent supply part 6, supply with pressurized air and urea water simultaneously to this nozzle 5, this nozzle 5 sprays supply after making the urea water atomizing.
Under this state, in Fig. 4, by the delivery temperature in the exhaust-gas upstream side of the being located at said nozzle 5 exhaust gas temperature sensor 9 detection outlet pipes 4 nearby, with this testing signal S
1Reducing agent supply control circuit 14 to reducing agent supply part 6 is sent.In addition, by being located at the internal pressure that detects these nozzles 5 to the pressure transducer midway 16 of the shared pipe arrangement 17 of nozzle 5, equally its testing signal S3 is sent to reducing agent supply control circuit 14.
At first, reducing agent supply control circuit 14 is used to the testing signal S from above-mentioned pressure transducer 16
3, the internal pressure of supervision nozzle 5 (below, abbreviate " pressing in the nozzle " as), judge whether it is authorized pressure P
1Or P
1More than (the step S11 of Fig. 5).At this moment, when causing the obstruction of nozzle 5, press liter in the nozzle by making, owing to preestablish the afore mentioned rules pressure P from air supplying tubing 12 supply pressurized air
1Pressure when stopping up for generation, thus can judge spray nozzle clogging by the rising of pressing in the nozzle.This moment, press less than authorized pressure P in the nozzle
1The time, judge spray nozzle clogging does not take place, then step S11 enters " NO " side, continues to monitor in the nozzle like this and presses.
Then, press in the nozzle to pressing P in the regulation
1Or P
1When above, step S11 enters " YES " side, enters step S12.At this, press P in the regulation to pressing in the nozzle to be continuously
1Or P
1The time of above state is carried out timing.And, judge to be continuously and press P in the regulation
1Or P
1Whether the time of above state is stipulated time t
1Or t
1More than (step S13).This be because, improve device reliability for the error of getting rid of pressure transducer 16 or misoperation etc., judge and press in the nozzle to pressing P in the regulation
1Or P
1Above state continuance be not less than as stipulated time t
1And after the value of setting, spray nozzle clogging has taken place.At this moment, the endurance is less than stipulated time t
1The time, judge spray nozzle clogging do not take place that step S13 enters " NO " side, enters step S14.And, judge once more whether pressure is to press P in the regulation in the nozzle
1Or P
1More than, enter " YES " side and monitor the endurance.
Then, the endurance is stipulated time t
1Or t
1When above, be judged as nozzle 5 and stop up, step S13 enters " YES " side, enters step S15.At this, close air supply valve 13 shown in Figure 4 and supply valve 11, stop nozzle 5 is supplied with pressurized air and supplied with urea water.Thus, the inside that suppresses said nozzle 5 is compressed air and urea water cooling, and by the exhaust heating of flowing in outlet pipe 4, the fixedly urea that solidifies in nozzle interior is melted.
Then, be used to testing signal S from exhaust gas temperature sensor shown in Figure 49
1, monitor nozzle 5 delivery temperature (being designated hereinafter simply as " nozzle is temperature nearby ") nearby, judge whether it is set point of temperature T
1Or T
1More than (step S16).At this moment, because the fusing point of solid urea is 132 ℃, so preestablish T
1Be not less than 132 ℃, can make the solid urea fusing in the said nozzle 5.At this moment, nozzle nearby temperature less than set point of temperature T
1The time, be judged as fixedly that urea can not melt, then step S16 enters " NO " side, continues to monitor nearby temperature of nozzle like this.
Then, temperature is set point of temperature T near the nozzle
1Or T
1When above, step S16 enters " YES " side, enters step S17.At this, to nozzle nearby temperature be continuously and be not less than set point of temperature T
1Time of state carry out timing.And, judge that it is continuously to be not less than set point of temperature T
1Time of state whether be stipulated time t
2Or t
2More than (step S18).This be because, improve device reliability for the error of getting rid of exhaust gas temperature sensor 9 or misoperation etc., have only nozzle nearby temperature be set point of temperature T
1Or T
1Above state continuance be not less than and be set at stipulated time t
2Value the time, just be judged as solid urea fusing.At this moment, the endurance is less than stipulated time t
2The time, being judged as solid urea and not melting, step S18 enters " NO " side, enters step S19.And, judge once more nozzle nearby temperature whether be set point of temperature T
1Or T
1More than, enter " YES " side and monitor the endurance.
Then, the endurance is stipulated time t
2Or t
2When above, be judged as the fixedly urea fusing in the nozzle 5, step S18 enters " YES " side, enters step S20.At this, open air supply valve 13 shown in Figure 4, begin again nozzle 5 is supplied with pressurized air.
And, judge whether pressure is another authorized pressure P in the nozzle
2Or P
2Below (step S21).At this moment, if the fusing of the solid urea in the nozzle 5 even then supply with pressurized air from air supplying tubing 12, is pressed in the nozzle and also can not risen from constant pressure, owing to be redefined for the afore mentioned rules pressure P
2For pressing in the nozzle that blocked state does not take place, so can judge by the reduction of pressing in the nozzle and eliminated spray nozzle clogging.At this moment, pressing in the nozzle is authorized pressure P
2Or P
2When following, be judged as by the fusing of solid urea and eliminated spray nozzle clogging, step S21 enters " YES " side, enters step S22.At this, open supply valve shown in Figure 4 11, begin again nozzle 5 is supplied with urea water.Thus, nozzle 5 reverts to the normal state that does not have obstruction.
On the other hand, another authorized pressure of nozzle inner pressure ratio P
2When high, be judged as solid urea and do not melt, do not eliminate spray nozzle clogging, step S21 enters " NO " side, at step S23 to the each increment of the counting of number of occurrence Ni " 1 ", judge number of occurrence Ni in predetermined stipulated number at step S24, then return above-mentioned steps S15.And, stop once more nozzle 5 is supplied with pressurized air and supplied with urea water, carry out above steps repeatedly, carry out the action of the elimination spray nozzle clogging of stipulated number.
At this moment,, when number of occurrence Ni has surpassed fixed number of times, enter " NO " side, carry out mistake output and handle (step S25), stop the supply system (step S26) of urea water, tenth skill at step S24.Thus, stop nozzle 5 is supplied with pressurized air and supplied with urea water, suppress nozzle interior and be cooled,, can be melted in the cakey fixedly urea of nozzle interior and eliminate spray nozzle clogging by exhaust heated nozzle 5 mobile outlet pipe 4 in.Therefore,, also can eliminate the obstruction of nozzle 5, improve the purified treatment efficient of NOx even the delivery temperature in the outlet pipe 4 is low.
Then, the running by motor 1 stops, and by the action of reducing agent supply part 6, at first blocks from storage tank 7 and supplies with urea water when nozzle 5 sprays urea water will finishing, and only supplies with pressurized air to nozzle 5 for the time being thereafter.Thus, blow out urea water, finish the injection of urea water from the spray orifice of nozzle 5 or the path that arrives this spray orifice.Like this,, can not be created in residual or so-called " the back drip " of the urea water when nozzle 5 stopped to supply with urea water, can prevent at spray orifice or arrive urea water crystallization in the path of this spray orifice and cause obstruction by blowing out urea water from nozzle 5.
In addition, in Fig. 4, though the pressure transducers 16 in the reducing agent supply part 6 be provided in a side of supply with pressurized air and shared pipe arrangement 17 from urea water to nozzle 5 midway, the present invention is not limited to this, also can be provided in the inside of nozzle 5, directly detect the internal pressure of this nozzle 5.
Claims (3)
1. the Exhaust gas purifying device of a motor comprises:
Reducing catalyst, it is equipped in the engine exhaust system, is used for reducing the nitrogen oxide of purifying exhaust gas with reducing agent;
The reducing agent supply part, it has nozzle, and this nozzle is supplied with reducing agent and pressurized air simultaneously, after this reducing agent atomizing, in the exhaust passageway of above-mentioned vent systems this reducing agent is sprayed supply to the exhaust-gas upstream side of above-mentioned reducing catalyst;
Temperature detection part, it is located near the exhaust-gas upstream side of said nozzle, is used to detect the delivery temperature in the exhaust passageway;
It is characterized in that, above-mentioned reducing agent supply part, be used to testing signal from the delivery temperature of said temperature detection part, the reducing agent delivery volume is set under its delivery temperature, said nozzle inside is cooled to be lower than the reducing agent crystallized temperature delivery volume lower limit or more than the lower limit, supply with reducing agent with this reducing agent delivery volume to this nozzle.
2. the Exhaust gas purifying device of motor according to claim 1 is characterized in that,
Above-mentioned reducing agent supply part has control circuit, this control circuit input is from the testing signal of the delivery temperature of said temperature detection part, and the signal of the operating condition of input motor, obtain the reducing agent delivery volume under this engine operating status, and obtain under its delivery temperature, said nozzle inside is cooled to be lower than the lower limit of the reducing agent delivery volume of reducing agent crystallized temperature, relatively the two sets the delivery volume of reducing agent.
3. the Exhaust gas purifying device of motor according to claim 1 and 2 is characterized in that, above-mentioned reducing agent is an aqueous solution of urea.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP344758/2003 | 2003-10-02 | ||
| JP2003344757A JP3732493B2 (en) | 2003-10-02 | 2003-10-02 | Engine exhaust purification system |
| JP344757/2003 | 2003-10-02 |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2008101106559A Division CN101328827B (en) | 2003-10-02 | 2004-09-13 | Exhaust gas purifying apparatus for engine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1863987A CN1863987A (en) | 2006-11-15 |
| CN100404808C true CN100404808C (en) | 2008-07-23 |
Family
ID=34538283
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2008101106559A Expired - Fee Related CN101328827B (en) | 2003-10-02 | 2004-09-13 | Exhaust gas purifying apparatus for engine |
| CNB2004800286338A Expired - Fee Related CN100404808C (en) | 2003-10-02 | 2004-09-13 | Exhaust gas cleaner for engine |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2008101106559A Expired - Fee Related CN101328827B (en) | 2003-10-02 | 2004-09-13 | Exhaust gas purifying apparatus for engine |
Country Status (3)
| Country | Link |
|---|---|
| JP (1) | JP3732493B2 (en) |
| CN (2) | CN101328827B (en) |
| ES (1) | ES2367485T3 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103003540A (en) * | 2010-06-21 | 2013-03-27 | 斯堪尼亚商用车有限公司 | Method and device pertaining to dosing unit of scr system |
Families Citing this family (28)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4673145B2 (en) * | 2005-06-24 | 2011-04-20 | 株式会社サムソン | Denitration device that automatically eliminates clogging of urea water injection nozzle |
| JP4949151B2 (en) | 2007-07-20 | 2012-06-06 | 三菱ふそうトラック・バス株式会社 | Exhaust gas purification device for internal combustion engine |
| JP4949152B2 (en) | 2007-07-20 | 2012-06-06 | 三菱ふそうトラック・バス株式会社 | Exhaust gas purification device for internal combustion engine |
| JP2009097438A (en) * | 2007-10-17 | 2009-05-07 | Mitsubishi Fuso Truck & Bus Corp | Exhaust emission control system |
| JP2009097479A (en) * | 2007-10-19 | 2009-05-07 | Bosch Corp | Device and method for controlling reducing agent supplying device |
| CN102105662B (en) * | 2008-07-07 | 2014-04-30 | 格兰富Nonox公司 | Dosing system for use in an exhaust system of a combustion engine |
| US8266894B2 (en) * | 2008-12-23 | 2012-09-18 | GM Global Technology Operations LLC | Thermal protection system for reducing agent injector |
| US20110036078A1 (en) * | 2009-08-14 | 2011-02-17 | International Engine Intellectual Property Company , Llc | Method for urea injection control |
| JP5091933B2 (en) * | 2009-10-01 | 2012-12-05 | 日立建機株式会社 | Exhaust purification device |
| JP5325850B2 (en) * | 2009-10-30 | 2013-10-23 | ボッシュ株式会社 | Abnormality detection device and abnormality detection method for reducing agent injection valve, and exhaust purification device for internal combustion engine |
| JP5678475B2 (en) * | 2010-05-25 | 2015-03-04 | いすゞ自動車株式会社 | SCR system |
| SE537642C2 (en) * | 2010-06-21 | 2015-09-08 | Scania Cv Ab | Method and apparatus for cooling a reducing agent dosing unit |
| SE534974C2 (en) * | 2010-06-21 | 2012-03-06 | Scania Cv Ab | Method and apparatus for determining the minimum level of a reducing agent container in an SCR system based on the cooling needs of a dosing unit |
| SE536316C2 (en) * | 2010-06-21 | 2013-08-20 | Scania Cv Ab | Method and apparatus for removing fuel from a metering unit of an HC metering system |
| CN102562237B (en) * | 2010-12-21 | 2016-06-08 | 中国第一汽车集团公司无锡油泵油嘴研究所 | The control method of addition amount of reducing agent in diesel engine tail gas treatment device |
| WO2012090800A1 (en) | 2010-12-27 | 2012-07-05 | ボッシュ株式会社 | Exhaust purification system and method for controlling exhaust purification system |
| US9261006B2 (en) * | 2013-03-01 | 2016-02-16 | Cummins Ip, Inc. | Apparatus, method and system for diagnosing reductant deposits in an exhaust aftertreatment system |
| US9234445B2 (en) * | 2013-06-06 | 2016-01-12 | Cummins Emission Solutions Inc. | Systems and techniques for nozzle cooling of diesel exhaust fluid injection systems |
| US9056279B1 (en) * | 2014-01-14 | 2015-06-16 | General Electric Company | Systems and methods for controlling emissions in an internal combustion engine through the control of temperature at the inlet of an ammonia slip catalyst assembly |
| JP2016094863A (en) | 2014-11-13 | 2016-05-26 | いすゞ自動車株式会社 | Urea water injection system and method of preventing crystallization of urea water injection device |
| KR102240005B1 (en) * | 2014-12-05 | 2021-04-14 | 두산인프라코어 주식회사 | Selective catalyst reduction system and method for reducing agent dosing module |
| DE102015016244A1 (en) * | 2015-12-16 | 2017-06-22 | Albonair Gmbh | Heat-resistant reducing agent injection nozzle |
| CN110645112B (en) * | 2019-09-29 | 2022-04-26 | 潍柴动力股份有限公司 | Engine failure detection method, device and engine |
| JP7254010B2 (en) * | 2019-11-19 | 2023-04-07 | 日立造船株式会社 | Hydrolysis system, denitrification equipment, and control method for hydrolysis system |
| CN112943420A (en) * | 2021-03-09 | 2021-06-11 | 广西玉柴机器股份有限公司 | Strategy for correcting urea injection amount to prevent urea from crystallizing |
| CN113294229B (en) * | 2021-05-08 | 2022-10-18 | 亿元达(天津)机电科技有限公司 | Energy-saving environment-friendly purifier for automobile |
| CN113982723A (en) * | 2021-09-30 | 2022-01-28 | 东风商用车有限公司 | Control method for urea nozzle protection |
| CN115217584B (en) * | 2022-03-01 | 2024-03-08 | 广州汽车集团股份有限公司 | Exhaust gas treatment device and exhaust gas treatment method for hydrogen engine, and vehicle |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003039718A1 (en) * | 2001-11-06 | 2003-05-15 | Robert Bosch Gmbh | Method and device for reducing nitrogen oxides present in exhaust gases |
| JP2003222019A (en) * | 2002-01-29 | 2003-08-08 | Toyota Motor Corp | Reducing agent supply device |
| JP2003269145A (en) * | 2002-03-11 | 2003-09-25 | Mitsubishi Fuso Truck & Bus Corp | NOx PURIFICATION DEVICE OF INTERNAL COMBUSTION ENGINE |
| JP2003269141A (en) * | 2002-03-11 | 2003-09-25 | Mitsui & Co Ltd | Reducing agent composition for flue gas denitration |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2088713C (en) * | 1992-02-24 | 1999-11-16 | Hans Thomas Hug | Cleaning exhaust gases from combustion installations |
| DE4436397B4 (en) * | 1994-10-12 | 2006-06-08 | Robert Bosch Gmbh | Device for aftertreatment of exhaust gases |
-
2003
- 2003-10-02 JP JP2003344757A patent/JP3732493B2/en not_active Expired - Lifetime
-
2004
- 2004-09-13 CN CN2008101106559A patent/CN101328827B/en not_active Expired - Fee Related
- 2004-09-13 ES ES04772987T patent/ES2367485T3/en not_active Expired - Lifetime
- 2004-09-13 CN CNB2004800286338A patent/CN100404808C/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003039718A1 (en) * | 2001-11-06 | 2003-05-15 | Robert Bosch Gmbh | Method and device for reducing nitrogen oxides present in exhaust gases |
| JP2003222019A (en) * | 2002-01-29 | 2003-08-08 | Toyota Motor Corp | Reducing agent supply device |
| JP2003269145A (en) * | 2002-03-11 | 2003-09-25 | Mitsubishi Fuso Truck & Bus Corp | NOx PURIFICATION DEVICE OF INTERNAL COMBUSTION ENGINE |
| JP2003269141A (en) * | 2002-03-11 | 2003-09-25 | Mitsui & Co Ltd | Reducing agent composition for flue gas denitration |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103003540A (en) * | 2010-06-21 | 2013-03-27 | 斯堪尼亚商用车有限公司 | Method and device pertaining to dosing unit of scr system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1863987A (en) | 2006-11-15 |
| CN101328827B (en) | 2011-04-06 |
| JP3732493B2 (en) | 2006-01-05 |
| CN101328827A (en) | 2008-12-24 |
| ES2367485T3 (en) | 2011-11-03 |
| JP2005113687A (en) | 2005-04-28 |
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Effective date of registration: 20220415 Address after: Gothenburg Patentee after: VOLVO TRUCK Corp. Address before: Saitama Prefecture, Japan Patentee before: UD Trucks Corp. Effective date of registration: 20220415 Address after: Saitama Prefecture, Japan Patentee after: UD Trucks Corp. Address before: Saitama Prefecture, Japan Patentee before: Nissan Diesel Motor Co.,Ltd. |
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Granted publication date: 20080723 |