JPH052812B2 - - Google Patents
Info
- Publication number
- JPH052812B2 JPH052812B2 JP57129265A JP12926582A JPH052812B2 JP H052812 B2 JPH052812 B2 JP H052812B2 JP 57129265 A JP57129265 A JP 57129265A JP 12926582 A JP12926582 A JP 12926582A JP H052812 B2 JPH052812 B2 JP H052812B2
- Authority
- JP
- Japan
- Prior art keywords
- valve
- particle collector
- exhaust gas
- particles
- particle
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
- F01N3/023—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles
- F01N3/027—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles using electric or magnetic heating means
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
- F01N3/031—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters having means for by-passing filters, e.g. when clogged or during cold engine start
- F01N3/032—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters having means for by-passing filters, e.g. when clogged or during cold engine start during filter regeneration only
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Processes For Solid Components From Exhaust (AREA)
Description
【発明の詳細な説明】
〓産業上の利用分野〓
本発明は、デイーゼル機関等の内燃機関に於て
排気ガス中の炭素粒子の如き粒子を捕捉する粒子
捕集器の再生方法に係る。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a method for regenerating a particle collector for capturing particles such as carbon particles in exhaust gas in an internal combustion engine such as a diesel engine.
〓従来の技術〓
デイーゼル機関に於て、その排気通路の途中
に、排気ガス中の炭素粒子の如き可燃性粒子を捕
捉してこれが大気中へ放出されることを防止する
粒子捕集器を設けることが従来から知られてい
る。〓Prior art〓 In a diesel engine, a particle collector is provided in the middle of the exhaust passage to trap combustible particles such as carbon particles in the exhaust gas and prevent them from being released into the atmosphere. This has been known for a long time.
粒子捕集器は、耐熱性の捕集材を有し、捕集し
た粒子の量が増大するに従つてその捕集材が詰ま
り、通気抵抗が増大し、正常な排気ガスの流れに
支障を来たすようになる。従つてデイーゼル機関
の正常な排気ガス流れに支障を来たすことなく粒
子捕集器が長期間に亙つて使用されるためには、
粒子捕集器に捕捉された粒子量が増大してときに
はこれを除去し、粒子捕集器の再生を行う必要が
ある。この粒子捕集器の再生は、該粒子捕集器の
捕捉粒子が炭素粒子等の可燃性であることから、
これを発火させて焼失灰化させることにより行う
ことが一般的であり、それには捕集材の上流側端
面部に電気式ヒータを設け、該電気式ヒータによ
り前記捕集材に付着している捕捉粒子をその上流
側端面部に付着している部分にて着火し、該捕捉
粒子の燃焼による火炎の伝播により捕集材の上流
側端部にある粒子より下流側端部にある粒子迄
次々に焼失灰化させる再生方法が既に提案されて
いる。 The particle collector has a heat-resistant collection material, and as the amount of collected particles increases, the collection material becomes clogged, increasing ventilation resistance and interfering with the normal flow of exhaust gas. It starts to come. Therefore, in order for a particle collector to be used for a long period of time without interfering with the normal exhaust gas flow of a diesel engine, it is necessary to
When the amount of particles trapped in the particle collector increases, it is necessary to remove them and regenerate the particle collector. This regeneration of the particle collector is carried out because the particles captured by the particle collector are flammable such as carbon particles.
This is generally done by igniting and incinerating the ash, and for this purpose, an electric heater is provided on the upstream end of the collection material, and the electric heater causes the material to adhere to the collection material. The captured particles are ignited at the part that is attached to the upstream end surface, and the flame propagation due to combustion of the captured particles causes the particles at the upstream end of the collection material to reach the particles at the downstream end one after another. A recycling method has already been proposed in which the waste is incinerated and ashed.
〓発明が解決しようとする課題〓
かかる粒子捕集器の再生方法に於ては、捕捉粒
子の着火が容易に且確実に行なわれることと、着
火後火炎の吹消えを来たすことなく火炎を良好に
且確実に伝播させることが重要である。〓Problems to be Solved by the Invention〓 In this method of regenerating a particle collector, the captured particles can be easily and reliably ignited, and the flame can be maintained in a good condition without causing the flame to blow out after ignition. It is important to ensure that the virus spreads quickly and reliably.
本発明は、捕捉粒子の焼失灰化による粒子捕集
器の再生に際して、捕捉粒子の着火を容易に且確
実に行い、更に着火後の火炎伝播を良好に且確実
に行うことができ、しかも内燃機関の運転性を阻
害することがない粒子捕集器の再生方法を提供す
ることを課題としている。 The present invention makes it possible to easily and reliably ignite the trapped particles when regenerating a particle collector by incinerating and ashing the trapped particles, and also to ensure good and reliable flame propagation after ignition. The object of the present invention is to provide a method for regenerating a particle collector that does not impede engine drivability.
〓課題を解決するための手段〓
かかる課題は、本発明によれば、粒子捕集器が
捕集した粒子を電気式ヒータにより着火させて該
粒子を焼失灰化せしめる粒子捕集器の再生方法に
して、前記粒子捕集器を流れる排気ガスの流量を
第一の弁により制御すると共に前記粒子捕集器と
前記第一の弁をバイパスして設けられたバイパス
通路を流れる排気ガスの流量を第二の弁により制
御し、再生時には前記粒子捕集器の入口部に設け
られた電気式ヒータに通電すると共に前記第一の
弁を全閉とし又前記第二の弁を全開とし、この状
態を前記粒子捕集器の入口部の温度が粒子の着火
を示す第一の所定温度に達する迄維持し、前記第
一の所定温度に達した後、前記第一の弁及び第二
の弁の開度を機関回転数と機関負荷とに応じて各
弁について予め設定されている開度に設定しつ
つ、この状態を前記粒子捕集器の出口部の温度が
該粒子捕集器の出口部迄火炎が到達したことを示
す第二の所定温度に達する迄維持し、前記第二の
所定温度に達した後、前記第一の弁を全開とし又
前記第二の弁を全閉とすることを特徴とする粒子
捕集器の再生方法によつて達成される。<Means for Solving the Problem> According to the present invention, the problem is solved by a method for regenerating a particle collector, in which the particles collected by the particle collector are ignited by an electric heater, and the particles are burned and incinerated. The flow rate of the exhaust gas flowing through the particle collector is controlled by a first valve, and the flow rate of the exhaust gas flowing through a bypass passage provided to bypass the particle collector and the first valve is controlled. During regeneration, the electric heater provided at the inlet of the particle collector is energized, the first valve is fully closed, the second valve is fully open, and this state is controlled by a second valve. is maintained until the temperature at the inlet of the particle collector reaches a first predetermined temperature indicating ignition of particles, and after reaching the first predetermined temperature, the first valve and the second valve are While setting the opening degree to a preset opening degree for each valve depending on the engine speed and engine load, this state is maintained such that the temperature at the outlet part of the particle collector is maintain the flame until it reaches a second predetermined temperature indicating that the flame has reached it, and after reaching the second predetermined temperature, fully open the first valve and fully close the second valve. This is achieved by a method for regenerating a particle collector characterized by the following.
〓発明の作用及び効果〓
捕捉粒子を電気式ヒータにより着火させるに
は、電熱の発生は酸素を要しないので、着火部を
なるべく冷さないのが好ましく、従つて着火部の
周りに空気の流れが生じていないのが好ましい。
従つて本発明の方法による如く、捕捉粒子の電気
式ヒータによる着火に際して、前記第一の弁を全
閉とし又前記第二の弁を全開とすることにより粒
子捕集器へのガス流を完全に遮断することは、捕
捉粒子の電気式ヒータによる着火に関して、特に
有効である。〓Operations and Effects of the Invention〓 In order to ignite the captured particles using an electric heater, since oxygen is not required to generate electric heat, it is preferable to keep the ignition part as cool as possible, and therefore, it is preferable to keep the ignition part as cool as possible. It is preferable that this does not occur.
Therefore, according to the method of the present invention, when the captured particles are ignited by the electric heater, the first valve is fully closed and the second valve is fully open, thereby completely preventing the gas flow to the particle collector. This is particularly effective with respect to ignition of captured particles by an electric heater.
粒子着火の安定度はその温度によつて検知する
のがその確実の点から特に有効である。 Detecting the stability of particle ignition based on its temperature is particularly effective in terms of reliability.
一旦所定の安定度を有する着火が達成された後
は、捕捉粒子を安定して燃焼させ又燃焼を粒子捕
集器の入口部より出口部へ可及的速かに進行させ
るには、或る最適の空気流が粒子捕集器を通つて
流されることが必要である。この場合、最適空気
流量は排気ガス中の酸素濃度によつて異なり、デ
イーゼル機関の排気ガス中の酸素濃度には機関の
運転状態、特に回転数と負荷が影響する。従つて
粒子捕集器再生中に粒子捕集器を通つて流す排ガ
ス流量を機関回転数と機関負荷に応じてプログラ
ム制御することは、捕捉粒子の燃焼による再生の
進行を最適化する上で特に有効である。 Once ignition with a predetermined stability is achieved, certain steps must be taken to stably burn the captured particles and to allow the combustion to proceed from the inlet to the outlet of the particle collector as quickly as possible. It is necessary that optimal airflow be directed through the particle collector. In this case, the optimum air flow rate varies depending on the oxygen concentration in the exhaust gas, and the oxygen concentration in the exhaust gas of a diesel engine is influenced by the operating state of the engine, particularly the rotation speed and load. Therefore, program control of the flow rate of exhaust gas flowing through the particle collector during particle collector regeneration according to the engine speed and engine load is especially effective in optimizing the progress of regeneration by burning the trapped particles. It is valid.
粒子捕集器内に於ける捕捉粒子の燃焼が粒子捕
集器の出口部迄達すると、この部分は火炎によつ
て温度が上昇するので、これを検出することによ
り粒子捕集器の再生が終了したのを逸早く確認で
き、これによつて前記第一の弁を全開とし、前記
第二の弁を全開とすることにより、粒子捕集器の
再生完了後早急に粒子捕集器の作動を全力復帰さ
せることができるので、再生のための粒子捕集器
の非稼動率を最低限に止めることができる。 When the combustion of the trapped particles in the particle collector reaches the outlet of the particle collector, the temperature of this part increases due to the flame, so by detecting this, the particle collector can be regenerated. It is possible to quickly confirm that the particle collector has been regenerated, and by fully opening the first valve and the second valve, the operation of the particle collector can be started immediately after the regeneration of the particle collector is completed. Since it is possible to return to full capacity, the non-operation rate of the particle collector for regeneration can be kept to a minimum.
〓実施例〓
以下に添付の図を参照して本発明を実施例につ
いて詳循細に説明する。〓Examples〓 The present invention will now be described in detail by way of embodiments with reference to the accompanying drawings.
第1図は本発明による粒子捕集器の再生方法を
実施する装置の一つの実施例を示す概略構成図で
ある。第1図に於て、1は入口管を、2は出口管
を各々示しており、入口管1は図示されていない
内燃機関の排気ポートに接続される。入口管1と
出口管2と粒子捕集器3によつて接続され、また
粒子捕集器3をバイパスしたバイパス管6によつ
て接続されている。 FIG. 1 is a schematic diagram showing one embodiment of an apparatus for carrying out the method for regenerating a particle collector according to the present invention. In FIG. 1, 1 indicates an inlet pipe, and 2 indicates an outlet pipe, and the inlet pipe 1 is connected to an exhaust port of an internal combustion engine (not shown). The inlet pipe 1 and the outlet pipe 2 are connected by a particle collector 3, and are also connected by a bypass pipe 6 that bypasses the particle collector 3.
粒子捕集器3は耐熱性のフオームフイルタ或い
はハニカムフイルタによつて構成された捕集材4
を有しており、該捕集材4はこれを通過する排気
ガス中の炭素粒子の如き粒子を捕捉するようにな
つている。捕捉材4の上流側端面部には電気式ヒ
ータ5が設けられており、該電気式ヒータ5には
バツテリ電源7の電流が電気スイツチ8を経て選
択的に供給されるようになつている。 The particle collector 3 has a collection material 4 made of a heat-resistant foam filter or honeycomb filter.
The collecting material 4 is adapted to capture particles such as carbon particles in the exhaust gas passing therethrough. An electric heater 5 is provided on the upstream end surface of the capture material 4, and a current from a battery power source 7 is selectively supplied to the electric heater 5 via an electric switch 8.
入口管1の粒子捕集器3に対する接続端近傍、
換言すれば粒子捕集器3の上流側近傍には弁9
が、またバイパス管6の途中には弁10が各々設
けられている。弁9及び10は各々弁軸11,1
2に担持されたバタフライ弁として構成され、ダ
イヤフラム装置13,14によつて各々個別に開
閉駆動されるようになつている。ダイヤフラム装
置13及び14は各々そのダイヤフラム室16,
17に負圧が導入されていない時には弁9及び1
0を全開位置にもたらし、これに対しダイヤフラ
ム室16,17に負圧が導入さている時には弁9
及び10を開弁させ、その負圧の増大に応じて弁
9及び10の開度を増大するようになつている。 Near the connection end of the inlet pipe 1 to the particle collector 3,
In other words, the valve 9 is located near the upstream side of the particle collector 3.
However, valves 10 are provided in the middle of the bypass pipes 6, respectively. Valves 9 and 10 have valve shafts 11 and 1, respectively.
It is constructed as a butterfly valve supported by a diaphragm device 13 and 14, and is individually driven to open and close by diaphragm devices 13 and 14, respectively. The diaphragm devices 13 and 14 each have a diaphragm chamber 16,
When negative pressure is not introduced to 17, valves 9 and 1
0 to the fully open position, whereas when negative pressure is introduced into the diaphragm chambers 16, 17, the valve 9
and 10 are opened, and the opening degrees of valves 9 and 10 are increased in accordance with the increase in negative pressure.
ダイヤフラム室16及び17は各々導管18,
19によつて負圧制御弁20,21のポートaに
接続されている。負圧制御弁20及び21は各々
ポートa以外に大気ポートbと負圧ポートcとを
有しており、負圧ポートcは導管22,23によ
つて図示されていない負圧ポンプに接続され、こ
れより負圧を与えられるようになつている。負圧
制御弁20及び21は電磁弁として構成され、負
圧制御弁20は通電時にはポートaを負圧ポート
cに接続し、非通電時にはポートaを大気ポート
bに接続し、これに対し負圧制御弁21は通電時
にはポートaを大気ポートbに接続し、非通電時
にはポートaを負圧ポートcに接続するようにな
つている。 Diaphragm chambers 16 and 17 each have a conduit 18,
19 to port a of the negative pressure control valves 20 and 21. In addition to port a, each of the negative pressure control valves 20 and 21 has an atmospheric port b and a negative pressure port c, and the negative pressure port c is connected to a negative pressure pump (not shown) through conduits 22 and 23. , which allows more negative pressure to be applied. Negative pressure control valves 20 and 21 are configured as electromagnetic valves, and negative pressure control valve 20 connects port a to negative pressure port c when energized, and connects port a to atmospheric port b when de-energized. The pressure control valve 21 connects port a to atmospheric port b when energized, and connects port a to negative pressure port c when de-energized.
25は制御装置を示している。制御装置25は
マイクロコンピユータ等を含む電気式のものであ
り、粒子捕集器3の排気ガス入口部に取付けられ
た温度センサ26より排気ガス温度に関する情報
を、また粒子捕集器3の排気ガス出口部に設けら
れた温度センサ27より排気ガス温度に関する情
報を、回転数センサ28より内燃機関の回転数に
関する情報を、負荷センサ29より内燃機関の負
荷に関する情報を各々与えられ、これら情報に応
じて電気スイツチ8の開閉及び負圧制御弁20,
21に対する通電を制御するようになつている。 25 indicates a control device. The control device 25 is an electric type including a microcomputer, etc., and receives information about the exhaust gas temperature from a temperature sensor 26 attached to the exhaust gas inlet of the particle collector 3, and also receives information about the exhaust gas from the particle collector 3. The temperature sensor 27 provided at the outlet receives information regarding the exhaust gas temperature, the rotation speed sensor 28 provides information regarding the rotation speed of the internal combustion engine, and the load sensor 29 provides information regarding the load of the internal combustion engine. to open/close the electric switch 8 and the negative pressure control valve 20,
21 is controlled.
次に第2図に示されたフローチヤートを参照し
て上述した如き構成からなる粒子排出防止装置の
作用に説明する。 Next, the operation of the particle emission prevention device constructed as described above will be explained with reference to the flowchart shown in FIG.
第2図に示されたフローチヤートのルーチンは
内燃機関の1回転毎に実行される。 The routine of the flowchart shown in FIG. 2 is executed every revolution of the internal combustion engine.
先ずステツプ1に於ては、温度センサ26,2
7、回転数センサ28、負荷センサ29より与え
られる情報の読込みが行われる。 First, in step 1, the temperature sensors 26, 2
7. Information provided by the rotation speed sensor 28 and load sensor 29 is read.
次にステツプ2に於ては、フラツグFが1であ
るか否かの判別が行われる。フラグF=1である
時には粒子捕集器3の再生が既に開始されている
時であり、フラツグF=1でない時にはまだ粒子
捕集器3の再生が行われていない時である。フラ
ツグF=1でない時にはステツプ3へ進み、この
ステツプに於ては、機関回転数の積算が行われ、
回転数積算値Nが求められる。 Next, in step 2, it is determined whether flag F is 1 or not. When the flag F=1, it means that regeneration of the particle collector 3 has already started, and when the flag F=1, it means that the regeneration of the particle collector 3 has not yet been started. When the flag F is not 1, the process proceeds to step 3, in which the engine speed is integrated.
The rotational speed integrated value N is determined.
次にステツプ4へ進み、このステツプに於ては
回転数積算値Nが所定値A以上であるか否かの判
別が行われる。N≧Aである時には粒子捕集器3
の再生を行うべき時期であり、N≧Aでない時に
はまだ粒子捕集器3の再生を行わなくても良い時
期である。N≧Aでない時にはステツプ1に戻
る。 Next, the process advances to step 4, in which it is determined whether the rotational speed integrated value N is greater than or equal to a predetermined value A. When N≧A, particle collector 3
This is the time when the particle collector 3 should be regenerated, and when N≧A is not satisfied, it is not necessary to regenerate the particle collector 3 yet. When N≧A is not satisfied, the process returns to step 1.
N≧Aである時にはステツプ5へ進み、このス
テツプに於ては、回転数積算値Nが零にリセツト
され、またフラツグFが1にセツトされる。 When N≧A, the routine advances to step 5, in which the rotational speed integrated value N is reset to zero and the flag F is set to 1.
次にステツプ6へ進み、このステツプに於て
は、電気スイツチ8SWに通電が行われ、また負
圧制御弁20(VCV1)と負圧制御弁21
(VCV2)に通電が行われる。これにより電気式
ヒータ5に通電が行われてこれが発熱し、ダイヤ
フラム室16に負圧が導入されて弁9が第1図に
於て仮想線で示されている如き全閉位置にもたら
され、またダイヤフラム室17に大気圧が導入さ
れ、弁10が第1図に於て仮想線で示されている
如き全開位置ににもたらされる。この時には粒子
捕集器3の補集材14の上流側端部と弁9の間に
閉じられた空間が構成され、該空間内に閉込めら
れた排気ガスが電気ヒータ5によつて加熱され
る。尚、この時には粒子捕集器3には排気ガスが
流れず内燃機関が排出する排気ガスは全てバイパ
ス管6を経て流れる。 Next, the process advances to step 6, in which the electric switch 8SW is energized, and the negative pressure control valve 20 (VCV1) and the negative pressure control valve 21 are energized.
(VCV2) is energized. This energizes the electric heater 5, which generates heat, introduces negative pressure into the diaphragm chamber 16, and brings the valve 9 to the fully closed position as shown by the imaginary line in FIG. Also, atmospheric pressure is introduced into the diaphragm chamber 17, bringing the valve 10 to the fully open position as shown in phantom in FIG. At this time, a closed space is formed between the upstream end of the collection material 14 of the particle collector 3 and the valve 9, and the exhaust gas trapped in this space is heated by the electric heater 5. Ru. Incidentally, at this time, no exhaust gas flows into the particle collector 3, and all exhaust gas discharged from the internal combustion engine flows through the bypass pipe 6.
ステツプ6の次はステツプ1へ戻り、ステツプ
2へ進む。この時にはフラツグF=1であるか
ら、ステツプ7へ進み、このステツプに於ては、
温度センサ26により検出された前記空間に於け
る排気ガス温度Tiが所定値Bより大きいが否か
の判別が行われる。T1=Bでない時にはステツ
プ1へ戻り、電気式ヒータ5に引続き通電が行わ
れ、弁9が全閉位置にあつて弁10が全開位置に
ある状態が維持される。 After step 6, return to step 1 and proceed to step 2. Since the flag F=1 at this time, the process advances to step 7, and in this step,
It is determined whether the exhaust gas temperature Ti in the space detected by the temperature sensor 26 is greater than a predetermined value B or not. When T 1 =B is not the case, the process returns to step 1, and the electric heater 5 is continuously energized to maintain the state in which the valve 9 is in the fully closed position and the valve 10 is in the fully open position.
T1≧Bである時は捕集材4の上流側端面部に
付着している粒子が前記空間に於ける排気ガスに
より着火された時であり、この時にはステツプ8
へ進み、このステツプに於ては、機関回転数と機
関負荷とに応じて予め記憶装置にストアされてい
る弁開度情報が回転数センサ28が検出する機関
回転数と負荷センサ29により検出された機関負
荷とに応じて読出される。 When T 1 ≧B, it means that the particles adhering to the upstream end surface of the collection material 4 are ignited by the exhaust gas in the space, and in this case, step 8
In this step, the valve opening degree information stored in advance in the storage device according to the engine speed and the engine load is detected by the engine speed detected by the engine speed sensor 28 and by the load sensor 29. It is read out according to the engine load.
次にステツプ9へ進み、このステツプに於て
は、電気スイツチ8が開かれて電気式ヒータ5に
対する通電が停止され、そして負圧制御弁20及
び21に前記弁開度情報に応じたデユーテイ比の
パルス信号が与えられる。これにより負圧制御弁
20及び21は共にパルス信号のデユーテイ比に
応じてポートaを大気ポートbと負圧ポートcと
に繰返し接続することにより、ダイヤフラム室1
6及び17には所定の負圧が導入され、弁9及び
10は共に所定の中間開度位置にもたらされる。
この時、弁9と10とは互いに相反する方向に駆
動され、即ち、弁9の開弁量が増大するとき弁1
0の開弁量が減少し、また弁9の開弁量が減少す
るとき弁10の開弁量が増大し、これにより粒子
捕集器3にはその時の内燃機関の運転状態に拘ら
ず所定流量の排気ガスが流れ、残りの排気ガスが
バイパス管6を経て流れる。上述の如く粒子捕集
器3を所定流量の排気ガスが流れることにより、
排気ガス中の酸素が捕集粒子の燃焼を促進し、ま
たその火炎がガス流れに乗つて下流側へ伝播し、
捕集材4が捕集している粒子が次々に焼失灰化す
る。このように弁9と10とによつて粒子捕集器
3を流れる排気ガス流量とバイパス管6を流れる
排気ガス流量とが制御されることにより、排気ガ
スの流れを阻害することなく粒子捕集器3にその
時の内燃機関の回転数、負荷に応じて前記記憶装
置にストアされた機関回転数と機関負荷に応じた
排気ガスが流れる。この排気ガス流量が粒子捕集
器3の再生時に於ける火炎伝播の促進に有効な比
較的小さい値に設設定されていることにより、粒
子捕集器3の再生が迅速に、また火炎の吹消えが
生じることなく確実に行なわれる。 Next, the process advances to step 9, in which the electric switch 8 is opened to stop energizing the electric heater 5, and the negative pressure control valves 20 and 21 are given a duty ratio according to the valve opening information. A pulse signal is given. As a result, the negative pressure control valves 20 and 21 repeatedly connect the port a to the atmospheric port b and the negative pressure port c according to the duty ratio of the pulse signal.
A predetermined negative pressure is introduced into valves 6 and 17, and both valves 9 and 10 are brought to a predetermined intermediate opening position.
At this time, valves 9 and 10 are driven in opposite directions, that is, when the opening amount of valve 9 increases, valve 1
When the opening amount of the valve 0 decreases and the opening amount of the valve 9 decreases, the opening amount of the valve 10 increases, which causes the particle collector 3 to have a predetermined amount of energy regardless of the operating state of the internal combustion engine at that time. A certain amount of exhaust gas flows, and the remaining exhaust gas flows through bypass pipe 6. As described above, when a predetermined flow rate of exhaust gas flows through the particle collector 3,
The oxygen in the exhaust gas promotes the combustion of the collected particles, and the flame propagates downstream along with the gas flow.
The particles collected by the collection material 4 are burned and incinerated one after another. By controlling the flow rate of exhaust gas flowing through the particle collector 3 and the flow rate of exhaust gas flowing through the bypass pipe 6 by the valves 9 and 10 in this way, particles can be collected without obstructing the flow of exhaust gas. Exhaust gas corresponding to the engine speed and engine load stored in the storage device flows into the engine 3 in accordance with the engine speed and engine load at that time. By setting the exhaust gas flow rate to a relatively small value that is effective for promoting flame propagation during regeneration of the particle collector 3, the regeneration of the particle collector 3 can be performed quickly and the flame can be blown. This is done reliably without any disappearance.
ステツプ9の次は、ステツプ10へ進み、この
ステツプに於ては温度センサ27によつて検出さ
れた粒子捕集器3より出る排気ガスの温度T0が
所定値C以上であるか否かの判別が行われる。
T0≧Cである時には捕集材4の後端部まで火炎
が到達し、これによつて粒子捕集器3より出る排
気ガスの温度が非常に高くなつて時であり、これ
によつて粒子捕集器3の再生が完了したと判別す
る。即ちT0≧Cである時にはステツプ11へ進
み、フラツグFを0とし、そして次にステツプ1
2へ進み、このステツプに於ては、負圧制御弁2
0,21に対する通電が停止される。この時には
ダイヤフラム室16に大気圧が導入されることに
より弁9は全開位置にもたらされ、ダイヤフラム
室17には負圧が導入されることにより弁10は
全閉位置にもたらされる。従つてこの時には排気
ガスの全てが粒子捕集器3を経て流れ、粒子捕集
器3により排気ガス中の粒子の捕集が再開され
る。 After step 9, the process proceeds to step 10, in which it is determined whether the temperature T0 of the exhaust gas coming out of the particle collector 3 detected by the temperature sensor 27 is equal to or higher than a predetermined value C. A determination is made.
When T 0 ≧C, the flame reaches the rear end of the particle collector 4, and the temperature of the exhaust gas coming out of the particle collector 3 becomes extremely high. It is determined that the regeneration of the particle collector 3 has been completed. That is, when T 0 ≧C, proceed to step 11, set flag F to 0, and then proceed to step 1.
2, and in this step, the negative pressure control valve 2
The power supply to 0 and 21 is stopped. At this time, atmospheric pressure is introduced into the diaphragm chamber 16 to bring the valve 9 to the fully open position, and negative pressure is introduced to the diaphragm chamber 17 to bring the valve 10 to the fully closed position. Therefore, at this time, all of the exhaust gas flows through the particle collector 3, and the particle collector 3 resumes collecting particles in the exhaust gas.
以上に於ては本発明を特定の実施例について詳
細に説明したが、本発明はこれに限定されるもの
ではなく、本発明の範囲内にて種々の実施例が可
能であることは当業者にとつて明らかであろう。 Although the present invention has been described in detail above with reference to specific embodiments, it is understood by those skilled in the art that the present invention is not limited thereto, and that various embodiments can be made within the scope of the present invention. It would be obvious to
第1図は本発明による粒子捕集器の再生方法を
実施する装置の一つの実施例を示す概略構成図、
第2図は本発明による粒子捕集器の再生方法の実
施要領を示すフローチヤートである。
1……入口管、2……出口管、3……粒子捕集
器、4……捕集材、5…電気式ヒータ、6……バ
イパス管、7……バツテリ電源、8……電気スイ
ツチ、9,10……弁、11,12……弁軸、1
3,14……ダイヤフラム装置、16,17……
ダイヤフラム室、18,19……導管、20,2
1……負圧制御弁、22,23……導管、25…
…制御装置、26,27……温度センサ、28…
…回転数センサ、29……負荷センサ。
FIG. 1 is a schematic configuration diagram showing one embodiment of an apparatus for carrying out the method for regenerating a particle collector according to the present invention;
FIG. 2 is a flowchart showing the procedure for regenerating a particle collector according to the present invention. 1... Inlet pipe, 2... Outlet pipe, 3... Particle collector, 4... Collection material, 5... Electric heater, 6... Bypass pipe, 7... Battery power supply, 8... Electric switch , 9, 10... Valve, 11, 12... Valve stem, 1
3, 14... diaphragm device, 16, 17...
Diaphragm chamber, 18, 19... Conduit, 20, 2
1... Negative pressure control valve, 22, 23... Conduit, 25...
...Control device, 26, 27...Temperature sensor, 28...
...Rotation speed sensor, 29...Load sensor.
Claims (1)
より着火させて該粒子を焼失灰化せしめる粒子捕
集器の再生方法にして、前記粒子捕集器を流れる
排気ガスの流量を第一の弁により制御すると共に
前記粒子捕集器と前記第一の弁をバイパスして設
けられたバイパス通路を流れる排気ガスの流量を
第二の弁により制御し、再生時には前記粒子捕集
器の入口部に設けられた電気式ヒータに通電する
と共に前記第一の弁を全閉とし又前記第二の弁を
全開とし、この状態を前記粒子捕集器の入口部の
温度が粒子の着火を示す第一の所定温度に達する
迄維持し、前記第一の所定温度に達した後、前記
第一の弁及び第二の弁の開度を機関回転数と機関
負荷とに応じて各弁について予め設定されている
開度に設定しつつ、この状態を前記粒子捕集器の
出力部の温度が該粒子捕集器の出口部迄火炎が到
達したことを示す第二の所定温度に達する迄維持
し、前記第二の所定温度に達した後、前記第一の
弁を全開とし又前記第二の弁を全閉とすることを
特徴とする粒子捕集器の再生方法。1. A method for regenerating a particle collector in which the particles collected by the particle collector are ignited by an electric heater to burn and incinerate the particles, and the flow rate of the exhaust gas flowing through the particle collector is set to a first level. and a second valve to control the flow rate of exhaust gas flowing through a bypass passage provided to bypass the particle collector and the first valve, and at the time of regeneration, the inlet portion of the particle collector is controlled by a second valve. At the same time, the first valve is fully closed and the second valve is fully opened, and this state is maintained until the temperature at the inlet of the particle collector indicates particle ignition. and after reaching the first predetermined temperature, the opening degrees of the first valve and the second valve are set in advance for each valve according to the engine speed and the engine load. and maintain this state until the temperature of the output part of the particle collector reaches a second predetermined temperature indicating that the flame has reached the outlet part of the particle collector. . A method for regenerating a particle collector, comprising fully opening the first valve and fully closing the second valve after reaching the second predetermined temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57129265A JPS5920514A (en) | 1982-07-23 | 1982-07-23 | Recycling method of particle collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57129265A JPS5920514A (en) | 1982-07-23 | 1982-07-23 | Recycling method of particle collector |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5920514A JPS5920514A (en) | 1984-02-02 |
| JPH052812B2 true JPH052812B2 (en) | 1993-01-13 |
Family
ID=15005295
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57129265A Granted JPS5920514A (en) | 1982-07-23 | 1982-07-23 | Recycling method of particle collector |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5920514A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58158310A (en) * | 1982-03-16 | 1983-09-20 | Nippon Soken Inc | Particulate purifier in exhaust gas of internal-combustion engine |
-
1982
- 1982-07-23 JP JP57129265A patent/JPS5920514A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5920514A (en) | 1984-02-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPS5928009A (en) | Fine particles purifying device for exhaust gas from diesel engine | |
| JPS59158313A (en) | Regenerative burner controller for exhaust micro particle catching trap for internal-combustion engine | |
| JPH0423091B2 (en) | ||
| JPS5920513A (en) | Method and equipment for preventing ejection of particles in internal combustion engine | |
| JP2926769B2 (en) | Exhaust gas purification device for internal combustion engine | |
| JPS638805Y2 (en) | ||
| JPS6319532Y2 (en) | ||
| JPH0771226A (en) | Exhaust particulate purifying device | |
| JPH0232450B2 (en) | ||
| JPS6319533Y2 (en) | ||
| JPS62159713A (en) | Exhaust gas purifying device for diesel engine | |
| JPH0627501B2 (en) | Exhaust particulate removal device for diesel engine | |
| JPS5920515A (en) | Recycling method of particle collector | |
| JP3580563B2 (en) | Exhaust gas particulate purification system for internal combustion engine | |
| JPS6325293Y2 (en) | ||
| JPH0517367B2 (en) | ||
| JP2797319B2 (en) | Particulate trap reburning device | |
| JPH0214523B2 (en) | ||
| KR0157853B1 (en) | Exhaust fine particle collection device of diesel engine | |
| JPH0432211B2 (en) | ||
| KR950011684B1 (en) | Diesel particulate combustion device using thin film heater | |
| JPH0513935Y2 (en) | ||
| JPH0480205B2 (en) | ||
| JPH0478809B2 (en) | ||
| JPH0134647Y2 (en) |