CN203584523U - Separated reversed-air-injecting regenerating type diesel engine exhausting particle catcher device - Google Patents
Separated reversed-air-injecting regenerating type diesel engine exhausting particle catcher device Download PDFInfo
- Publication number
- CN203584523U CN203584523U CN201320805153.4U CN201320805153U CN203584523U CN 203584523 U CN203584523 U CN 203584523U CN 201320805153 U CN201320805153 U CN 201320805153U CN 203584523 U CN203584523 U CN 203584523U
- Authority
- CN
- China
- Prior art keywords
- regeneration
- outlet
- main
- regenerating
- filter
- 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 - Fee Related
Links
- 230000001172 regenerating effect Effects 0.000 title claims abstract description 28
- 239000002245 particle Substances 0.000 title abstract description 18
- 238000001914 filtration Methods 0.000 claims abstract description 47
- 238000011069 regeneration method Methods 0.000 claims description 92
- 230000008929 regeneration Effects 0.000 claims description 90
- 239000000463 material Substances 0.000 claims description 12
- 238000000926 separation method Methods 0.000 claims description 7
- 239000000919 ceramic Substances 0.000 claims description 6
- 229910052878 cordierite Inorganic materials 0.000 claims description 6
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 claims description 6
- 239000000956 alloy Substances 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 4
- 238000011144 upstream manufacturing Methods 0.000 claims description 4
- 229910045601 alloy Inorganic materials 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 description 15
- 230000008439 repair process Effects 0.000 description 12
- 238000005516 engineering process Methods 0.000 description 9
- 239000013618 particulate matter Substances 0.000 description 9
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 5
- 239000002956 ash Substances 0.000 description 5
- 230000032683 aging Effects 0.000 description 4
- 238000013461 design Methods 0.000 description 4
- 238000005485 electric heating Methods 0.000 description 4
- 125000004122 cyclic group Chemical group 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 241001676635 Lepidorhombus whiffiagonis Species 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- 238000013459 approach Methods 0.000 description 2
- 229910010293 ceramic material Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 238000012958 reprocessing Methods 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000012052 concurrent chemoradiation therapy Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000011118 depth filtration Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000013467 fragmentation Methods 0.000 description 1
- 238000006062 fragmentation reaction Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 210000004072 lung Anatomy 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 229910021653 sulphate ion Inorganic materials 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Landscapes
- Processes For Solid Components From Exhaust (AREA)
Abstract
The utility model provides a separated reversed-air-injecting regenerating type diesel engine exhausting particle catcher device which comprises a main filtering system, a regenerating filtering system, an air injecting system and a control system. The main filtering system is composed of two inlet valves, an inlet expanding pipe, a main filtering body, an outlet collapsible tube, two air injecting electromagnetic valves, two outlet valves, a separating board and a main outlet pipe. The regenerating filtering system is located below the main filtering system and is composed of two regenerating inlet valves, a regenerating inlet pipe, a regenerating filtering body, a regenerating outlet pipe and a regenerating outlet valve. The air injecting system is composed of an air pump and an air storage tank. The control system is mainly composed of two pressure sensors and a controller. According to the separated reversed-air-injecting regenerating type diesel engine exhausting particle catcher device, the durability of the filtering body of the diesel engine exhausting particle catcher device can be improved by separating the filtering body, and emission at a regenerating stage is reduced.
Description
Technical field
The utility model relates to a kind of diesel engine particulate catcher device, is specifically related to a kind of separation type reverse jet regenerating formula diesel engine particulate catcher device.
Background technique
Pellet is the important composition of pollution of atmosphere, and pellet can be suspended in atmosphere for a long time, is easily deposited in lung, even enters blood, very big to harm.According to investigations, in the air of Beijing, 20% pellet derives from vehicular emission, and in fact, than petrol engine, diesel particulation (PM) discharge amount is 30-80 times of petrol engine.Therefore, improving diesel emission is the important channel that solves the pollution problem of Inhalable Particulate.
In order to meet the Abgasgesetz of increasingly stringent, further solving diesel particulate emission problem needs two technology paths: the one, and emission controls by improving combustion scheme; The 2nd, the outer reprocessing scheme of machine.Wherein, diesel engine particles catcher (Diesel particle filter, DPF) is approach most effectively in the outer reprocessing scheme of machine.Diesel engine particles catcher by inertial collision, hold back, the method such as diffusion and gravitational settling separates exhaust particulate from air-flow.The filtration mechanism of diesel engine particles catcher has a lot, as Electrostatic Absorption method, Mist Using Filtering and Capturing Method, centrifugal separation etc.Wherein using maximum is the honeycomb ceramic filter catcher in Mist Using Filtering and Capturing Method, by front and back, replaces shutoff, exhaust is therefrom passed, and particle is stayed in catcher.The technological core of diesel engine particles catcher comprises two aspects: filter material and filter regeneration techniques.
Diesel engine particles catcher filter material has a lot, and filter efficiency is good instantly, use many, cost is low, technology is the most ripe is cordierite honeycomb ceramic filter, but steinheilite poor thermal conductivity, regenerative process is its high temperature ageing easily.For this reason, silicon carbide honeycomb ceramics filter is considered to solution, but cost is relatively high.Meanwhile, the foamed alloy filter thermal conductivity of metal base is good, be applicable to carrying out thermal regeneration, but cost is higher equally.
Diesel engine particles catcher is after filtering after a while, and exhaust particulate, through in-depth filtration, can enter cake layer stationary operational phase, but along with the thickening of cake layer, the exhaust back pressure of catcher can raise gradually, causes gas exhaust piping droop loss, worsens diesel engine condition.Need to use various regeneration techniqueses to remove the particulate matter being accumulated in filter for this reason.Instantly main regeneration method mainly divides two kinds of passive regeneration and initiative regenerations.Cyclic regeneration in passive regeneration technology, as in CRT, CCRT technology, combines with DOC, in Europe, is used widely.But the anti-sulphur aging quality of cyclic regeneration technology used catalyst is poor, be not suitable for the current oil conditions of China.Active regeneration techniques, as the technology such as electric heating regeneration and oil spout regeneration can increase energy consumption greatly, and likely causes secondary pollution.
It is exactly that regenerative process cannot be removed non-flammable particulate matter that above regeneration method exists a common issue.In fact, in exhaust particulate, have 6% to be the metal ion oxide that sulphate or other fuel oils, lube oil additive form, these materials that are called as " ashes " cannot be eliminated by heating and catalytic process, can only regularly pass through manual method (pressurized air, high pressure water) and remove.Ashes delay in grain catcher can cause diesel car fuel oil Economy to worsen, and Europe experiment shows, after cyclic regeneration catcher is used 80,000 kilometers, because ashes material stops up, causes average fuel consumption to rise about 12%.China's diesel oil sulphur content is more much higher than Europe, and therefore in exhaust particulate, sulphates content is higher, and oil consumption is risen can be faster.
In diesel engine particles catcher active regeneration techniques, also have a kind of method to be called reverse jet regenerating technology.This technology is just proposed by Japan as far back as eighties of last century the nineties.This technology is by separation with filter PM burning, and when needs are regenerated, high pressure air sprays at a high speed from filter outlet, direction is contrary with exhaust, deposition PM removes from filter surface, enters special trap, then by electric heating or other firing units, PM is burnt.This method can be removed non-combustible ashes, the high temperature ageing that can avoid filter thermal regeneration to cause simultaneously.But traditional design thinking structure complexity, and reverse jet pressure is to this system regeneration effectiveness affects maximum, therefore desired jet bleed pressure is large, and in addition, puff prot biasing causes jet inhomogeneous, also causes regeneration efficiency not high.To sum up various reasons, this thinking is not used widely.The mechanisms such as domestic Tsing-Hua University, University Of Tianjin, Jilin University, Beijing Jiaotong University, military traffic institute had carried out correlative study in recent years.But the reverse jet regenerating system of developing still has problems: in the reverse jet system regeneration process of single-filtering body, undressed exhaust meeting is directly discharged into atmosphere, and this process will continue 15-30 minute, pollutes; The reverse jet system of two filter returns particulate matter blowback to combusted cylinder, can worsen like this environment in cylinder, and to diesel engine, work causes negative effect.
Summary of the invention
The utility model, for the deficiencies in the prior art, has proposed a kind of separation type reverse jet regenerating formula diesel engine particulate catcher device.
The technological scheme that the utility model technical solution problem is taked is:
The utility model comprises main filtration system, regeneration filtration system, gas ejecting system and control system.
Described main filtration system is comprised of two inlet valves, an entrance expanding duct, a main filter, an outlet collapsible tube, two solenoid valve doors, two outlet valves, a dividing plate and a primary outlet pipe; The osculum end of entrance expanding duct is arranged side by side two inlet valves, the big opening end of entrance expanding duct connects one end of main filter, one side of two outlet valves of another termination of main filter, the big opening end of the opposite side exit collapsible tube of two outlet valves, primary outlet pipe of osculum termination of outlet collapsible tube; On described outlet collapsible tube, be also provided with two solenoid valve doors; A dividing plate is divided into two-part of sealing each other by the entrance expanding duct of whole main filtration system, main filter and outlet collapsible tube, and wherein main filter material is cordierite honeycomb ceramic.
Described regeneration filtration system is positioned at main filtration system below, by two regeneration inlet valves, a regeneration inlet duct, a regeneration filter, a regeneration outer pipe and a regeneration outlet valve composition, regeneration inlet duct connects the entrance expanding duct of main filtration system by two regeneration inlet valves, regeneration outer pipe connects the primary outlet pipe of main filtration system by a regeneration outlet valve, a regeneration filter is set between regeneration inlet duct and regeneration outer pipe, described regeneration filter connects electric heater, can carry out thermal regeneration, the filter material of wherein regenerating is foamed alloy.
Described gas ejecting system is comprised of air pump, gas holder, and the air outlet of air pump connects the air intake of gas holder, and the air outlet of gas holder connects two solenoid valves of main filtration system.
Described control system is mainly comprised of two pressure transducers and controller.Two pressure transducers lay respectively at the upstream and downstream pipeline of whole device, two pressure sensor signals are exported to controller, and controller is also being controlled all valves, regeneration all valves of filtration system and the air pump of electric heater and gas ejecting system of main filtration system.
The beneficial effects of the utility model:
1. main filter, import expanding duct and outlet collapsible tube are become to two-part by baffle for separating.The advantage of spaced apart is, when main filter is wherein in the situation of part regeneration, another part still can normally be worked.Compared with single-filtering body reverse jet regenerating scheme, spaced apart scheme has effectively been avoided the pollution causing in regenerative process; Compared with two filter reverse jet regenerating schemes, spaced apart scheme is only used a filter, greatly reduces cost, has dwindled the volume of catcher.
2. a regeneration filter has been installed, and has connected main filter entrance expanding duct with regeneration inlet pipe, with regenerating, outer pipe is connected primary outlet pipe.Such arrangement is effectively filtered the air-flow that is mingled with the particulate matter coming off in main filter in regenerative process in regeneration filter, and carries out electric heating regeneration in regeneration filter.Meanwhile, because regeneration outer pipe is connected primary outlet pipe, can utilize due to main filter another part primary outlet pipe low pressure area of forming of high velocity air producing of normally working, the negative pressure that this region forms forms suction to the air-flow in regeneration filter pipeline, can reduce regeneration whiff pressure, effectively reduce the high request of reverse jet system to whiff pressure.Reduced the emission problem in regenerative process simultaneously.Compared with the particulate matter blowback back-steam cylinder that comes off reverse jet being produced with two filter schemes, the design's thinking can not worsen diesel engine condition.
3. better utilize filter material.The cordierite honeycomb ceramic material that main filter user cost is low, because regenerative heating process does not carry out in main filter, therefore can not cause the heat ageing of cordierite honeycomb ceramic material, has greatly improved the durability of main filter; Regeneration filter is used the better foamed alloy material of thermal conductivity, although this material cost is higher, regeneration filter relative volume is less, and materials are less, meanwhile, change and become comparatively easy, and cleaning ashes are very convenient.
4. adopt the low design proposal of the high outlet of entrance.Such design form be conducive to regenerate entrance and jet entrance more approaches main filter shaft axis, makes the jet particulate matter that comes off more easily enter regeneration inlet pipe, also makes jet more evenly, can increase reverse jet regenerating efficiency.
Accompanying drawing explanation
Fig. 1 a and Fig. 1 b are the three-dimensional profile structural drawing of this device.
Fig. 2 is the plan view of this device.
Fig. 3 is this device take Fig. 2 from right to left as the side view of direction of observation.
Fig. 4 is that this device is as A-A sectional drawing in Fig. 2 and Fig. 3.
Fig. 5 is a schematic diagram, represents system each several part composition that the utility model forms and the relation with other devices that are connected.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail.
The utility model relates to a kind of separation type reverse jet regenerating formula diesel engine particulate catcher device.This device front end connects the exhaust outlet of diesel engine by pipeline, rear end is connecting other after-treatment device by pipeline.Whole device comprises four parts: main filtration system, regeneration filtration system, gas ejecting system and control system.
Main filtration system is comprised of two inlet valves, an entrance expanding duct, a main filter, an outlet collapsible tube, two solenoid valve doors, two outlet valves and a primary outlet pipe, in addition, also have a dividing plate that the entrance expanding duct of whole main filtration system, main filter and outlet collapsible tube are divided into two-part of sealing each other.Wherein main filter material is cordierite honeycomb ceramic, and two-part that outlet collapsible tube is separated by dividing plate 10 are respectively equipped with a solenoid valve.
Regeneration filtration system is comprised of two regeneration inlet valves, a regeneration inlet duct, a regeneration filter, a regeneration outer pipe and a regeneration outlet valve.Wherein, regeneration inlet duct is connected the entrance expanding duct of main filtration system, and regeneration outer pipe is connected the regeneration outer pipe of main filtration system.In addition, regeneration filter connects electric heater, can carry out thermal regeneration.
Gas ejecting system is comprised of air pump, gas holder.Wherein, gas holder is connected two solenoid valves of main filtration system, and air pump is communicated with atmosphere.
Control system is mainly comprised of two pressure transducers and controller.Wherein, two pressure transducers lay respectively at the upstream and downstream pipeline of diesel engine particles catcher, controller is connecting two pressure transducers, in addition also connect and controlling all valves of main filtration system, all valves and the electric heater of regeneration filtration system, and the air pump of gas ejecting system.
As shown in Fig. 1 a, Fig. 1 b, Fig. 2, Fig. 3, Fig. 4 and Fig. 5, under normal operation, the tail gas that diesel engine 30 is discharged enters diesel engine particles catcher 31 through inlet valve 01 and inlet valve 02, and through entrance expanding duct 11 and 12, enter main filter 13 and 14 two-part and filter, through outlet valve 07 and 08, enter outlet collapsible tube 15 and 16 afterwards, pass through again primary outlet pipe 17, leave diesel engine particles catcher 31 and enter other after-treatment device 32(as DOC, SCR etc.) carry out next step vent gas treatment.During this period, be positioned at the pressure transducer 41 and the constantly exhaust pressure of this position of detection of pressure transducer 42 that is positioned at diesel engine particles catcher 31 downstreams of diesel engine particles catcher 31 upstreams, through controller 40, calculate droop loss.
When droop loss reaches the threshold values setting in advance, device is opened regeneration mode.By controller 40, control valvular switching, and in turn main filter 13 and 14 is carried out to reverse jet regenerating.
When device enters regeneration mode, first main filter 13 is carried out to reverse jet regenerating.Now, inlet valve 01, outlet valve 07 is closed, regeneration inlet valve 03, regeneration outlet valve 09 is opened, be stored in solenoid valve door 05(that pressurized air in gas holder 52 controls continuous opening and closing via controller 40 this moment solenoid valve door 06 close all the time) form pulsing airflow, through outlet collapsible tube, 15(has expanding duct effect this moment for reverse jet), enter main filter 13, the main filter 13 of backward erosion, and formation vibrations, make the particulate matter of main filter 13 deep layers get back to surface, and along with surface has formed the particulate matter fragmentation of cake layer, come off, pass through together entrance expanding duct 11, regeneration inlet valve 03 and regeneration inlet duct 20 enter into regeneration filter 21, through regeneration filter 21, filter, through regeneration outer pipe 22 and regeneration outlet valve 09, enter into primary outlet pipe 17, the exhaust of the next autonomous filter 14 of discharging with outlet valve 08 enters other after-treatment device 32.
The time of regenerative process is controlled by controller 40.After the regenerative process of main filter 13 finishes, inlet valve 01, outlet valve 07 are opened, and regeneration inlet valve 03, regeneration outlet valve 09 are closed, and jet valve 05 is in normally off, and afterwards, controller 40 can be controlled main filter 14 and regenerate.The regenerative process of main filter 14 is identical in principle with main filter 13 regenerative processes, therefore repeats no more.After main filter 13 and 14 two-part regenerative processes all finish, solenoid valve door 05 and 06 is in normally off, inlet valve 01 and 02, outlet valve 07 and 08 are all opened, and regeneration inlet valve 03 and 04 is all closed, and main filter 13 and 14 is all normally worked.
Afterwards, controller 40 is controlled electric heater 23 regeneration filter 21 is carried out to electric heating, and in the filter 21 that makes to regenerate, the particulate matter of accumulation burn totally, closes electric heater 60, closes afterwards the outlet valve 09 of regenerating.Controller 40 is controlled air pump 51 extracting air from atmosphere environment 50, and is stored in gas holder 52, makes gas holder air pressure be returned to regenerative process and starts previous state.The regenerative process of whole device all finishes.
Claims (1)
1. a separation type reverse jet regenerating formula diesel engine particulate catcher device, is characterized in that: comprise main filtration system, regeneration filtration system, gas ejecting system and control system;
Described main filtration system is comprised of two inlet valves, an entrance expanding duct, a main filter, an outlet collapsible tube, two solenoid valve doors, two outlet valves, a dividing plate and a primary outlet pipe; The osculum end of entrance expanding duct is arranged side by side two inlet valves, the big opening end of entrance expanding duct connects one end of main filter, one side of two outlet valves of another termination of main filter, the big opening end of the opposite side exit collapsible tube of two outlet valves, primary outlet pipe of osculum termination of outlet collapsible tube; On described outlet collapsible tube, be also provided with two solenoid valve doors; A dividing plate is divided into two-part of sealing each other by the entrance expanding duct of whole main filtration system, main filter and outlet collapsible tube, and wherein main filter material is cordierite honeycomb ceramic;
Described regeneration filtration system is positioned at main filtration system below, by two regeneration inlet valves, a regeneration inlet duct, a regeneration filter, a regeneration outer pipe and a regeneration outlet valve composition, regeneration inlet duct connects the entrance expanding duct of main filtration system by two regeneration inlet valves, regeneration outer pipe connects the primary outlet pipe of main filtration system by a regeneration outlet valve, a regeneration filter is set between regeneration inlet duct and regeneration outer pipe, described regeneration filter connects electric heater, can carry out thermal regeneration, the filter material of wherein regenerating is foamed alloy,
Described gas ejecting system is comprised of air pump, gas holder, and the air outlet of air pump connects the air intake of gas holder, and the air outlet of gas holder connects two solenoid valves of main filtration system;
Described control system is mainly comprised of two pressure transducers and controller; Two pressure transducers lay respectively at the upstream and downstream pipeline of whole device, two pressure sensor signals are exported to controller, and controller is also being controlled all valves, regeneration all valves of filtration system and the air pump of electric heater and gas ejecting system of main filtration system.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320805153.4U CN203584523U (en) | 2013-12-09 | 2013-12-09 | Separated reversed-air-injecting regenerating type diesel engine exhausting particle catcher device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320805153.4U CN203584523U (en) | 2013-12-09 | 2013-12-09 | Separated reversed-air-injecting regenerating type diesel engine exhausting particle catcher device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN203584523U true CN203584523U (en) | 2014-05-07 |
Family
ID=50582459
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201320805153.4U Expired - Fee Related CN203584523U (en) | 2013-12-09 | 2013-12-09 | Separated reversed-air-injecting regenerating type diesel engine exhausting particle catcher device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN203584523U (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103670606A (en) * | 2013-12-09 | 2014-03-26 | 浙江大学 | Separation-type reverse air injection regenerative diesel engine exhaust particle filter device |
CN105697105A (en) * | 2016-04-21 | 2016-06-22 | 北京高鑫伟业滤清器有限责任公司 | Filter disc |
CN112627942A (en) * | 2020-10-27 | 2021-04-09 | 蓝晶卡特排放技术南京有限公司 | Regeneration method and system of diesel particulate filter |
-
2013
- 2013-12-09 CN CN201320805153.4U patent/CN203584523U/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103670606A (en) * | 2013-12-09 | 2014-03-26 | 浙江大学 | Separation-type reverse air injection regenerative diesel engine exhaust particle filter device |
CN103670606B (en) * | 2013-12-09 | 2016-01-20 | 浙江大学 | Separation-type reverse air injection regenerative diesel engine exhaust particle filter device |
CN105697105A (en) * | 2016-04-21 | 2016-06-22 | 北京高鑫伟业滤清器有限责任公司 | Filter disc |
CN105697105B (en) * | 2016-04-21 | 2020-07-17 | 北京高鑫伟业滤清器有限责任公司 | Filter disc |
CN112627942A (en) * | 2020-10-27 | 2021-04-09 | 蓝晶卡特排放技术南京有限公司 | Regeneration method and system of diesel particulate filter |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104454084B (en) | A kind of pulse cleaning eddy flow trap | |
CN103670606B (en) | Separation-type reverse air injection regenerative diesel engine exhaust particle filter device | |
CN204060865U (en) | A kind of pulse cleaning eddy flow catcher | |
CN100395435C (en) | Wall flow type net plate apparatus with reverse jet regenerating unit for collecting microparicle discharged by diesel vehicle | |
US5930994A (en) | Reverse cleaning regeneration type exhaust emission control device and method of regenerating the same | |
CN107747505B (en) | System for regenerating DPF (diesel particulate filter) alternately by utilizing engine exhaust and control method | |
CN203584524U (en) | Back-blowing type exhaust smoke purification device | |
CN203584523U (en) | Separated reversed-air-injecting regenerating type diesel engine exhausting particle catcher device | |
KR20140048131A (en) | Wet exhaust gas purification device | |
CN103184947A (en) | Control device and control method of diesel engine | |
CN107842412A (en) | The renovation process and system of a kind of diesel particulate trap | |
JP6539551B2 (en) | EXHAUST GAS TREATMENT APPARATUS, METHOD OF TEMPERATURE TEMPERATURE FOR CATALYST, METHOD FOR REGENERATING HONEYCOMB STRUCTURE AND METHOD FOR REMOVING ASH | |
CN104594982A (en) | Auxiliary regeneration device of vehicle particle catcher | |
CN208564700U (en) | A kind of marine diesel DPF, SCR intelligent integral smoke discharging and purifying device | |
CN203925695U (en) | The control system of engine exhaust temperature | |
CN102477886A (en) | Particle filtering device and regenerating method thereof | |
CN101405487B (en) | Exhaust gas purification device for internal combustion engine | |
CN106948906A (en) | A kind of hydrocarbon spraying system from supercharging | |
CN205370693U (en) | Binary channels tail gas throttle diesel engine DPF oil spout regenerating unit | |
CN203655390U (en) | Automatic regeneration system for DPF (diesel particulate filter) | |
CN108561210A (en) | Marine diesel pollutant emission processing system | |
CN204476519U (en) | Auxiliary regeneration device of vehicle particle catcher | |
CN115142936A (en) | Optimization analysis method for energy-saving regeneration of ash content of vehicle catalyst | |
JP2007332906A (en) | Dpf regeneration device of internal combustion engine | |
CN212508478U (en) | Diesel engine exhaust particle trapping and regenerating device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140507 Termination date: 20211209 |