JP5407288B2 - Exhaust gas treatment device and exhaust gas treatment method - Google Patents

Description

  The present invention relates to an exhaust gas processing apparatus and an exhaust gas processing method, and more particularly to an exhaust gas processing apparatus and an exhaust gas processing method provided with an SCR catalyst that reduces NOx in exhaust gas with ammonia and purifies it. .

Various proposals have been made to use an SCR (Selective Catalytic Reduction) catalyst using urea in order to purify nitrogen oxides (NOx) in the exhaust gas using the exhaust gas of the engine as a processing device. In such an exhaust gas treatment device, NOx in the exhaust gas is selectively adsorbed on the SCR catalyst, urea water is injected into the exhaust passage upstream of the SCR catalyst, and urea in the urea water is hydrolyzed and reduced. Ammonia (NH ₃ ) as an agent is supplied to the SCR catalyst, and NOx adsorbed on the SCR catalyst is reduced and decomposed into nitrogen and water and discharged.

  However, in such an exhaust gas processing apparatus for an engine, when the exhaust gas at the time of starting the engine is at a low temperature, the urea water injected into the exhaust passage on the upstream side of the SCR catalyst does not vaporize and enters the exhaust passage. There is a possibility of accumulation. Further, when urea is at a hydrolysis temperature (130 to 180 ° C.) or lower, the ammonia generation rate in which the urea is decomposed in the exhaust passage to become ammonia is extremely low, and the NOx purification rate is extremely low. In addition, undecomposed urea may pass through the SCR catalyst and be released into the atmosphere.

  In order to solve the low ammonia generation rate when the exhaust gas is low at the time of starting the engine, the urea water is not injected when the exhaust gas is low, and the exhaust gas temperature is set to be equal to or higher than the hydrolysis temperature of urea. When a certain threshold value is exceeded, urea water is injected by a target amount in a short time to prevent a decrease in the ammonia production rate. In this case, when the exhaust gas temperature is equal to or lower than the threshold value, NOx purification is performed. The problem of not being done remains.

  In addition, pre-adsorption in which ammonia is adsorbed to the SCR catalyst in advance before stopping the engine is effective, but the amount of ammonia adsorbed depends on the state when the engine is stopped. May be.

  Moreover, it is conceivable to use ammonia water or liquid ammonia instead of urea water, but these are highly toxic and difficult to handle. Because there are many users of vehicles equipped with an exhaust gas treatment device that uses an SCR catalyst, they do not have deep knowledge in handling ammonia water or liquid ammonia water, so use ammonia water or liquid ammonia. That is not realistic.

  Thus, in order to improve the ammonia production rate from urea at low temperature, it has been proposed to provide a hydrolysis catalyst upstream of the SCR catalyst. An exhaust gas purification system in which a urea supply nozzle, a urea hydrolysis catalyst, and an SCR catalyst are arranged in order from the side, and an exhaust gas purification system in which a silicon nitride surface is formed on a contact surface with the exhaust gas of the urea hydrolysis catalyst is disclosed. ing.

JP 2006-212591 A

However, in the technique of providing a urea hydrolysis catalyst as disclosed in Patent Document 1, an exhaust gas treatment apparatus is manufactured in which the entire exhaust gas treatment apparatus is increased in size and weight by providing the hydrolysis catalyst. There is a problem that the cost of doing so is high.
Furthermore, although the decomposition of urea is promoted by providing a hydrolysis catalyst, a sufficient ammonia production rate cannot be obtained and it is difficult to solve the conventional problems.

  Therefore, in view of the problems of the prior art, the present invention provides an exhaust gas processing apparatus and an exhaust gas processing method capable of improving the ammonia production rate from urea and improving the NOx purification rate when the exhaust gas temperature at the start of the engine is low. The purpose is to provide.

In order to solve the above problems, in the present invention, on the exhaust passage of the engine, a pre-stage oxidation catalyst for increasing the oxidation activity of NO in the exhaust gas in order from the upstream side, and an SCR catalyst for reducing NOx in the exhaust gas with ammonia In the exhaust gas treatment device that has a post-stage oxidation catalyst for removing ammonia and adds urea water between the pre-stage oxidation catalyst and the SCR catalyst, the temperature of the exhaust gas is the first during the normal operation of the engine. A control means is provided for adding urea water at a predetermined temperature or higher and adding urea water at a second predetermined temperature lower than the first predetermined temperature when the engine is started.
Further, the second predetermined temperature is a hydrolysis temperature of urea.
By providing the first control means for adding urea water at a second predetermined temperature below lower than the predetermined temperature the addition of urea water during normal operation, that early addition of the urea water since the start of the engine And the NOx purification rate can be improved.

Further, the second predetermined temperature is equal to or higher than an evaporation temperature of the urea water.
As a result, a NOx purification rate approximately twice that of normal control can be obtained.
Furthermore, since the urea water is not added until the exhaust gas temperature reaches the evaporation temperature of the urea water from the start of the engine, a part of the urea water does not vaporize and accumulates in the exhaust passage, and a part of the urea enters the exhaust passage. It can prevent adhering.

Further, the present invention is characterized in that there is provided a second control means for performing control for raising the temperature of the exhaust gas until the temperature of the exhaust gas reaches the hydrolysis temperature of urea.
Until the hydrolysis temperature of urea, in order to control the temperature of the exhaust gas to be increased, urea water is added from the start of the engine, the urea water decomposes, and the time until ammonia can be stably supplied to the SCR catalyst, That is, it is possible to shorten the time from when the engine is started until NOx can be stably purified.
As a result, urea water supplied to the SCR catalyst is quickly decomposed into ammonia, which is the original reducing agent of the SCR catalyst, and combined with the addition of urea water early after the engine starts, NOx is about three times that of normal control. A purification rate is obtained.
By using such control means, ammonia can be supplied at an early stage from the start of the engine, and the exhaust gas of the engine can be processed with a high NOx purification rate.

Further, when the temperature of the exhaust gas reaches the evaporation temperature of the urea water, to commence injection of the urea water, the injection of the urea water Tokoro quantification, the temperature of the exhaust gas is terminated before reaching the hydrolysis temperature of the urea As described above, control is performed by the control means.
Thereby, when the exhaust gas temperature reaches the hydrolysis temperature of urea, the addition of urea water is completed, so the ammonia production rate is improved, and the added urea water is used more effectively.

Further, an exhaust throttle valve capable of adjusting the flow rate of the exhaust gas is provided on the exhaust passage of the engine and upstream of the pre-stage oxidation catalyst, and the exhaust gas temperature is adjusted by adjusting the opening of the exhaust throttle valve. The temperature is increased.
An exhaust throttle valve is often provided on an exhaust passage of a general engine. Therefore, by adjusting the opening degree of the exhaust throttle valve and performing exhaust gas temperature increase control, the present invention can be implemented without greatly changing the existing system.

In addition, a map representing the relationship between the amount of ammonia that can be adsorbed on the SCR catalyst and the temperature is prepared, and the addition amount of the urea water is determined according to the exhaust gas temperature using the map.
This makes it possible to determine the appropriate amount of urea water added, so-called ammonia slip in which ammonia produced by hydrolysis of urea passes through the SCR catalyst and is released to the atmosphere does not occur. An amount of ammonia effective for NOx purification can be secured.

Furthermore, as an invention of a method for realizing the problem, the oxidation activity of NO in the exhaust gas is increased by the pre-stage oxidation catalyst, the NOx in the exhaust gas is reduced with ammonia by the SCR catalyst, and urea water is added. In the exhaust gas treatment method in which ammonia is removed by a post-stage oxidation catalyst, when the engine is started, a predetermined amount of urea water is injected at a temperature equal to or lower than the hydrolysis temperature of urea and equal to or higher than the evaporation temperature of urea water. At the same time, control is performed to raise the exhaust gas temperature until the temperature of the exhaust gas reaches the hydrolysis temperature of urea.

  As described above, according to the present invention, there is provided an exhaust gas processing apparatus and an exhaust gas processing method capable of improving the ammonia production rate from urea and improving the NOx purification rate even at low engine exhaust gas temperature. can do.

  Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the drawings. However, the dimensions, materials, shapes, relative arrangements, and the like of the components described in this embodiment are not intended to limit the scope of the present invention unless otherwise specified, but are merely illustrative examples. Not too much.

  FIG. 1 is a schematic diagram of an exhaust gas treatment apparatus according to the first embodiment. An outline of the exhaust gas treatment apparatus will be described with reference to FIG. As shown in FIG. 1, the exhaust treatment apparatus 1 of the present invention includes a DPF system 10 including a front-stage oxidation catalyst 2 and a filter 4, and an SCR system 12 including an SCR catalyst 6 and a rear-stage oxidation catalyst 8.

  In such an exhaust gas treatment device that combines the DPF system 10 and the SCR system 12, the exhaust gas generated in the engine 30 is first sent to the DPF system 10 including the pre-stage oxidation catalyst 2 and the filter 4, and the filter 4 performs PM (Particulate) Matter) is collected and discharged.

The exhaust gas after PM is collected by the filter 4 passes through the intermediate passage 14 and is sent to the SCR catalyst 6 constituting the SCR system 12. Further, urea water is injected from a urea injection nozzle 16 provided in the intermediate passage 14, and the urea in the urea water is decomposed to generate NH ₃ . The amount of urea water injected from the urea injection nozzle 16 is controlled by a control device 32 described later.

NH ₃ produced by decomposition of the urea water is once adsorbed on the SCR catalyst 6 and then reacts with NOx in the exhaust gas by the following reaction formulas (1) to (3) to harm noxious NOx. To N ₂ .
2NO + 2NO ₂ + 4NH ₃ → 4N ₂ + 6H ₂ O (1)
4NO + 4NH ₃ + O ₂ → 4N ₂ + 6H ₂ O (2)
6NO ₂ + 8NH ₃ → 7N ₂ + 12H ₂ O (3)

Furthermore, NH ₃ that could not be reacted with the SCR catalyst 6 reacted similarly with NOx that could not be reacted with the SCR catalyst 6 and the subsequent oxidation catalyst 8 according to the same reaction formulas (1) to (3) as the SCR catalyst 6. , Convert NOx to harmless N2. Further, NH ₃ adsorbed on the SCR catalyst 6 is desorbed from the SCR catalyst 6 due to the temperature rise, and is converted into N ₂ by the reaction equation (4) at the subsequent oxidation catalyst.
12NH ₃ + 9O ₂ → 6N ₂ + 18H ₂ O (4)

Next, the control by the control device 32 will be described with reference to FIG.
FIG. 2 is a flowchart of control by the control device 32 when the engine is started in the first embodiment.

  When the engine 30 is started in step S <b> 1, an engine start signal is sent from the engine 30 to the control device 32.

  When an engine start signal is sent in step S1, the controller 32 detects the temperature detected by the thermometer 18 that detects the temperature in the intermediate passage 14 located downstream of the DPF system 10 and upstream of the SCR system 12. T1 is acquired, and it is determined whether or not it is a cold start based on the temperature T1. The cold start is a start at a low temperature, and this is determined by whether or not the temperature T1 is equal to or lower than the decomposition temperature of urea. That is, if T1 is lower than the decomposition temperature of urea, it is a cold start, and if T1 is higher than the decomposition temperature of urea, it is not a cold start.

  If it is determined No in step S2, that is, it is not a cold start, the process proceeds to step S3 and normal control is performed.

If YES in step S2, that is, a cold start is determined, the urea water injection control surrounded by the dotted line A and the temperature increase control surrounded by the dotted line B in FIG. The urea water injection control and the temperature increase control are simultaneously performed in parallel . Here, the urea water injection control surrounded by a dotted line A will be described.

If it is determined Yes in step S2, the urea water injection control determines whether or not the temperature T1 detected by the thermometer 18 in step S11 is equal to or higher than the urea water evaporation temperature Ta. The urea water evaporation temperature Ta is a temperature at which the urea water evaporates, and is about 80 to 120 ° C. although it varies depending on the urea concentration, urea injection speed, amount, and the like.

  If it is determined No in step S11, step S11 is repeated until the temperature T1 rises by a temperature control described later, and becomes equal to or higher than the evaporation temperature Ta of the urea water.

  If it is determined Yes in step S11, the opening of the urea injection nozzle 16 is adjusted in step S12, and injection of urea water into the intermediate passage 14 is started.

When the injection of urea water is started in step S12, the ammonia map is referred to and it is determined whether or not the required amount of urea water is injected in step S13.
FIG. 4 shows an example of the ammonia map. In the ammonia map of FIG. 4, the vertical axis represents the amount of ammonia that can be adsorbed to the SCR catalyst 6, and the horizontal axis represents temperature. As shown in FIG. 4, ammonia is more adsorbed on the SCR catalyst 6 as the temperature is lower. Therefore, when the detection value at the previous engine stop of the thermometer 18 and T _E, the SCR catalyst 6 is believed that ammonia alone A _E is already adsorbed. Further, the adsorbable amount of ammonia on the SCR catalyst 6 at the current exhaust gas temperature T1 is A1. Therefore, ammonia can be newly adsorbed by A1−A _E = A, and urea water corresponding to A can be injected, and this value is set as the necessary amount of urea water in step S13.

If it is determined No in step S13, the urea injection is continued until the required amount of urea water is injected.
If it is determined Yes in step S13, the process proceeds to step S3, and normal control is performed for urea injection.

Next, the temperature rise control surrounded by the dotted line B will be described.
If it is determined Yes in step S2, in the temperature increase control, in step S21, the opening degree of the exhaust throttle valve 34 provided at the exhaust outlet of the engine is adjusted to be small, and the exhaust gas is forcibly heated. .
In this embodiment, the temperature of the exhaust gas is raised by adjusting the opening of the exhaust throttle valve 34. However, in step S21, other methods may be used as long as the temperature of the exhaust gas can be raised, for example, the engine The intake air can be throttled or the exhaust gas can be heated by providing a heater in the exhaust line.

When the temperature rise is started in step S21, it is determined in step S22 whether or not the temperature T1 detected by the thermometer 18 is equal to or higher than the urea decomposition temperature Tb. The urea decomposition temperature Tb is a temperature at which urea is hydrolyzed to ammonia, and is about 130 to 180 ° C. although it varies depending on the urea decomposition performance of the SCR.

  If it is determined No in step S22, the temperature T1 rises, and the temperature rise is continued until the temperature becomes equal to or higher than the urea decomposition temperature Tb.

  If it is determined Yes in step S22, the forced temperature rise is stopped in step S23, and the process proceeds to step S3.

FIG. 3 shows an example of temporal changes in the urea water injection amount and the exhaust gas temperature T1 during the control in the control device 32 described with reference to the flowchart of FIG.
FIG. 3 is a graph showing temporal changes in the exhaust gas temperature and the urea water injection amount at the start of the engine in the first embodiment. The vertical axis represents the urea water injection amount and temperature, and the horizontal axis represents time.

An example of the control described with reference to the flowchart of FIG. 2 will be described again along the time axis with reference to FIG.
As shown in FIG. 3, when the engine is cold-started at time 0, the temperature increase control is started. When the exhaust gas temperature T1 rises by the temperature increase control and reaches the urea water evaporation temperature Ta at time ta, the urea water injection is started. When the target amount of urea water is injected at time tc, the urea water injection is started. Stop. Thereafter, when the exhaust gas temperature T1 reaches the urea decomposition temperature Tb at time tb, that is, when the SCR temperature is low and the adsorptive urea is decomposed into ammonia, the temperature increase control is stopped, and thereafter normal control is performed.
Incidentally, in Examples and reverse 3, than the time tb when the exhaust gas temperature T 1 is reached to the urea decomposition temperature Tb, but towards the time tc the injection of the urea water is completed there may be later that when ammonia Since the generation rate is inferior, it is preferable to set the time tc ahead of the time tb as shown in FIG.

The control described in FIGS. 2 and 3 was performed under the normal control and the following six conditions 2 to 7, and the NOx purification rate at the start of the engine in the SCR catalyst 6 was examined.
Condition 1. Normal control conditions Urea early addition temperature: 25 ° C
Condition 3. Urea early addition temperature: 100 ° C
Condition 4. Urea early addition temperature: 130 ° C
Condition 5. 5. Urea early addition temperature: 130 ° C., temperature rise control: up to 180 ° C. 6. Urea early addition temperature: 130 ° C., temperature rise control: up to 200 ° C. Urea apparatus addition temperature: 130 ° C., temperature increase control: up to 130 ° C. Conditions 2 to 4 did not perform temperature increase control, and changed the early addition start timing (temperature) of urea.
Conditions 5 to 7 were the same except for the end timing of the temperature raising control.
The results are shown in FIG.
In FIG. 5, the vertical axis represents the NOx purification rate, and the horizontal axis represents the condition name.
As shown in FIG. 5, the NOx purification rate of the SCR catalyst 6 is greatly improved by the control, and a purification rate of 40%, which is about 2 years of normal control, can be obtained only by the early addition of urea. Even under the conditions, a NOx purification rate of 50% or more and a maximum of 60% was obtained.

(Comparative example)
FIG. 6 is a graph showing temporal changes in the exhaust gas temperature and the urea water injection amount when the engine is started in the comparative example. The vertical axis represents the urea water injection amount and temperature, and the horizontal axis represents time.
In the comparative example, the exhaust gas was not forcedly heated after the engine was cold started. Further, when the exhaust gas temperature reached the urea water injection threshold set to be higher than the urea decomposition temperature, a target amount of urea water was added. This is a conventional control.
At this time, the NOx purification rate when the engine was started was about 20 to 30%.

According to the present invention, since the urea water is not added until the exhaust gas temperature reaches the evaporation temperature of the urea water from the start of the engine, the urea water does not vaporize and accumulate in the exhaust passage, and the urea water is not added. Up to the decomposition temperature, in order to control the temperature of the exhaust gas to rise, urea water is added from the start of the engine, the time from when the urea water decomposes and ammonia can be stably supplied to the SCR catalyst, that is, the engine The time from the start until NOx can be stably purified can be shortened.
Therefore, it can be said that ammonia can be supplied to the SCR catalyst at an early stage from the start of the engine, and the exhaust gas of the engine can be processed with a high NOx purification rate.

  In view of the problems of the prior art, the present invention is used as an exhaust gas processing apparatus and an exhaust gas processing method capable of improving the ammonia production rate from urea and improving the NOx purification rate at the time of engine start exhaust gas low temperature. can do.

1 is a schematic diagram of an exhaust gas treatment device in Embodiment 1. FIG. 3 is a flowchart of control by the control device at the time of engine start in the first embodiment. 6 is a graph showing temporal changes in exhaust gas temperature and urea water injection amount when the engine is started in the first embodiment. It is an example of an ammonia map. 4 is a graph showing the results of NOx purification rate in Example 1. It is a graph showing the time change of the exhaust gas temperature at the time of the engine start in a comparative example, and urea water injection amount.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Exhaust gas processing apparatus 2 Pre-stage oxidation catalyst 4 Filter 6 SCR catalyst 8 Post-stage oxidation catalyst 14 Intermediate passage 16 Urea water injection nozzle 18 Thermometer 30 Engine 32 Control apparatus 34 Exhaust throttle valve

Claims (4)

On the exhaust path of the engine, there are a pre-stage oxidation catalyst that increases the oxidation activity of NO in the exhaust gas in order from the upstream side, an SCR catalyst that reduces NOx in the exhaust gas with ammonia, and a post-stage oxidation catalyst that removes ammonia. In the exhaust gas treatment device for adding urea water between the pre-stage oxidation catalyst and the SCR catalyst,
Cold start determination means for determining whether the temperature of the exhaust gas downstream of the upstream oxidation catalyst and upstream of the SCR catalyst is equal to or lower than a second predetermined temperature that is a hydrolysis temperature of urea;
When the cold start determination means determines that the temperature of the exhaust gas is higher than the second predetermined temperature, the temperature of the exhaust gas downstream of the pre-stage oxidation catalyst and upstream of the SCR catalyst is the second temperature. Adding urea water at a first predetermined temperature higher than the predetermined temperature of
When the cold start determination means determines that the temperature of the exhaust gas is equal to or lower than the second predetermined temperature, the temperature of the exhaust gas downstream of the preceding oxidation catalyst and upstream of the SCR catalyst is the evaporation temperature of urea water. Above, and urea water injection control means for adding urea water below the second predetermined temperature;
When the cold start determination means determines that the temperature of the exhaust gas is equal to or lower than the second predetermined temperature, the temperature of the exhaust gas reaches the second predetermined temperature in parallel with the urea water injection control. An exhaust gas processing apparatus, comprising: a temperature increase control means for performing control to increase the temperature of the exhaust gas until The urea solution injection control means, when the temperature of the exhaust gas reaches the evaporation temperature of the urea water, to commence injection of the urea water, the injection of the urea water Tokoro quantification, temperature urea hydrolysis temperature of the exhaust gas The exhaust gas processing device according to claim 1, wherein the exhaust gas processing device is terminated before reaching. An exhaust throttle valve capable of adjusting the flow rate of the exhaust gas is provided on the exhaust passage of the engine and on the upstream side of the pre-stage oxidation catalyst,
The exhaust gas processing apparatus according to claim 1 or 2 , wherein the temperature raising control means raises the temperature of the exhaust gas by adjusting an opening of the exhaust throttle valve. Prepare a map showing the relationship between the amount of ammonia adsorbable on the SCR catalyst and the temperature of the exhaust gas,
The urea water injection control means uses the map to add the amount of urea water to be added when the cold start determination means determines that the temperature of the exhaust gas is higher than the second predetermined temperature. The exhaust gas processing device according to any one of claims 1 to 3, wherein the exhaust gas processing device is determined according to a temperature of the exhaust gas.

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