High-power diesel engine tail gas denitration SCR system gas mixing arrangement peculiar to vessel
Technical field
The present invention relates to a kind of high-power diesel engine tail gas denitration SCR system gas mixing arrangement peculiar to vessel, especially a kind of mixing efficiency that improves tail gas and urea in the diesel engine exhaust gas purification device that relates to is avoided the device of urea crystals.
Background technique
Conventional diesel engine exhaust gas purification device has does not have this mixing arrangement; But through the lengthening pipeline or increase the mixability of tail gas and urea; This mode pipeline that extends has at first increased cost, and in addition, long pipeline has increased the loss of exhaust temperature; Make urea produce crystallization easily, thereby influence the efficient of tail gas clean-up.What mixing arrangement was housed in addition also is the single-stage turbomixer, and such mixer can only be used in the exhaust environment of little caliber, when being applied to the big caliber environment of high-power diesel engine, the urea sedimentation can occur, mix phenomenons such as inhomogeneous.
Summary of the invention
The objective of the invention is to overcome above-mentioned deficiency; A kind of high-power diesel engine tail gas denitration SCR system gas mixing arrangement peculiar to vessel is provided; This gas mixer can be under the situation of cost and the loss of minimizing tail gas temperature that practices every conceivable frugality; Tail gas and urea are fully mixed, increase their surface of contact, improve the device of its transformation efficiency.
According to technological scheme provided by the invention; High-power diesel engine tail gas denitration SCR system gas mixing arrangement peculiar to vessel comprises air inlet pipeline, one group of mixing arrangement; Said one group of mixing arrangement by two independently mixer combine, said two independently mixer be installed in parallel in the mounting hole place of air inlet pipeline.
Said two independently mixer structure is identical, one of them independently mixer comprise cirque body, first guide plate, second guide plate, the 3rd guide plate, the 4th guide plate, the 5th guide plate, the 6th guide plate; What first guide plate, second guide plate, the 3rd guide plate, the 4th guide plate, the 5th guide plate, the 6th guide plate were parallel to each other is embedded in the cirque body, and length has nothing in common with each other between first guide plate, second guide plate, the 3rd guide plate, the 4th guide plate, the 5th guide plate, the 6th guide plate.
As further improvement of the present invention, the said first guide plate front end is outstanding, and first guide plate is provided with the flow-disturbing fin.
As further improvement of the present invention, the said second guide plate front end is outstanding, and second guide plate is provided with flow-disturbing fin and processus aboralis guide plate.
As further improvement of the present invention, said the 3rd guide plate front end is outstanding, and the 3rd guide plate is provided with flow-disturbing fin and processus aboralis guide plate.
As further improvement of the present invention, said the 4th guide plate front end is outstanding, and the 4th guide plate is provided with flow-disturbing fin and processus aboralis guide plate.
As further improvement of the present invention, said the 5th guide plate front end is outstanding, and the 5th guide plate is provided with flow-disturbing fin and processus aboralis guide plate.
As further improvement of the present invention, said the 6th guide plate front end is outstanding, and the 6th guide plate is provided with flow-disturbing fin, preceding prominent spoiler and processus aboralis spoiler.
Compared with present technology the present invention has the following advantages:
Structure of the present invention is simple relatively, compact, rationally; Adopt and seethe mixing up and down, be fit to big caliber multiphase flow and mix; By two mixer superpositions, carry out two-stage and mix, strengthen tail gas in the mixed effect of urea, make gas through the time upset its flow direction, it is fully mixed with urea; Easily manufactured, the practical row that is prone to; Thoroughly having solved tail gas and urea can not well-mixed drawback before reaction, thereby has guaranteed the surface of contact of tail gas and urea, has improved tail gas clean-up efficient.
Description of drawings
Fig. 1 is mounting arrangement schematic representation in the air inlet pipeline of the present invention.
Fig. 2 is a schematic perspective view of the present invention.
Fig. 3 is the present invention's first deflector structure schematic representation.
Fig. 4 is the present invention's second deflector structure schematic representation.
Fig. 5 is the present invention's the 3rd deflector structure schematic representation.
Fig. 6 is the present invention's the 4th deflector structure schematic representation.
Fig. 7 is the present invention's the 5th deflector structure schematic representation.
Fig. 8 is the present invention's the 6th deflector structure schematic representation.
Embodiment
Following the present invention will combine the embodiment in the accompanying drawing to further describe:
As shown in Figure 1; Comprise that high-power diesel engine tail gas denitration SCR system gas mixing arrangement peculiar to vessel comprises air inlet pipeline 1, one group of mixing arrangement 2; Said one group of mixing arrangement 2 by two independently mixer combine, said two independently mixer be installed in parallel in mounting hole 3 places of air inlet pipeline 1.
Shown in Fig. 2~8 figure, said two independently mixer structure is identical, one of them independently mixer comprise cirque body 4, first guide plate 5, second guide plate 6, the 3rd guide plate 7, the 4th guide plate 8, the 5th guide plate 9, the 6th guide plate 10; What first guide plate 5, second guide plate 6, the 3rd guide plate 7, the 4th guide plate 8, the 5th guide plate 9, the 6th guide plate 10 were parallel to each other is embedded in the cirque body 4, and length has nothing in common with each other between first guide plate 5, second guide plate 6, the 3rd guide plate 7, the 4th guide plate 8, the 5th guide plate 9, the 6th guide plate 10.
Said first guide plate, 5 front ends are outstanding, and first guide plate 5 is provided with flow-disturbing fin 11.
Said second guide plate, 6 front ends are outstanding, and second guide plate 6 is provided with flow-disturbing fin 12 and processus aboralis guide plate 13.
Said the 3rd guide plate 7 front ends are outstanding, and the 3rd guide plate 7 is provided with flow-disturbing fin 14 and processus aboralis guide plate 15.
Said the 4th guide plate 8 front ends are outstanding, and the 4th guide plate 8 is provided with flow-disturbing fin 16 and processus aboralis guide plate 17.
Said the 5th guide plate 9 front ends are outstanding, and the 5th guide plate 9 is provided with flow-disturbing fin 18 and processus aboralis guide plate 19.
Said the 6th guide plate 10 front ends are outstanding, and the 6th guide plate 10 is provided with flow-disturbing fin 21, preceding prominent spoiler 20 and processus aboralis spoiler 22.
Working principle of the present invention and working procedure:
After tail gas gets in the air inlet pipeline 1 and to mix with urea among the present invention; Because the urea straying quatity is bigger, can not be decomposed into NH3 rapidly, thereby multiphase flow in air inlet pipeline, occur; Urea deposits is in lower stream of airflow; When one group of mixing arrangement 2, the bottom tail gas that 20 pairs of the preceding prominent spoilers of mixer bottom guide plate 10 are rich in urea carries out sufficient flow-disturbing, through the processus aboralis guide plate of each guide plate 6~10 13,15,17,19,22 urea is fully mixed in tail gas again.Mixing can't reach well-mixed tail gas through one-level, mixes once more through second level mixer to have reached well-mixed purpose again.
The present invention has not only improved mixing efficiency, thereby improves transformation efficiency, has practiced thrift the cost of pipeline, and has saved the space, work under the environment that is more suitable for being restricted in spaces such as boats and ships.