CN203874588U - Twin-jet spraying-flushing dust-cleaning device - Google Patents

Twin-jet spraying-flushing dust-cleaning device Download PDF

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Publication number
CN203874588U
CN203874588U CN201420260979.1U CN201420260979U CN203874588U CN 203874588 U CN203874588 U CN 203874588U CN 201420260979 U CN201420260979 U CN 201420260979U CN 203874588 U CN203874588 U CN 203874588U
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China
Prior art keywords
spraying
carrier pipe
flushing
filter core
blowing gas
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CN201420260979.1U
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Chinese (zh)
Inventor
朱书成
赵家亮
李金峰
庞志峰
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Henan Longcheng Coal Efficient Technology Application Co Ltd
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Henan Longcheng Coal Efficient Technology Application Co Ltd
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Abstract

The utility model discloses a twin-jet spraying-flushing dust-cleaning device. The device comprises two spraying-flushing gas delivery pipes and a spraying-flushing pipe, wherein one spraying-flushing gas delivery pipe is connected with an upper nozzle above a filter element of a dust collector, and the other spraying-flushing gas delivery pipe is connected with a lower nozzle under the filter element of the dust collector; the spraying-flushing gas delivery pipe for supplying gas to the lower nozzle is connected with a dust-containing gas inlet pipe of the dust collector, and the spraying-flushing gas delivery pipe for supplying gas to the upper nozzle is connected with a gas outlet pipe of a gas purifying chamber of the dust collector or an external gas supply device. According to the twin-jet spraying-flushing dust-cleaning device, a mode of combining internal-spraying and back-flushing and bottom external-spraying separating of the filter element of the dust collector is adopted, and the spraying-flushing temperature and spraying-flushing mode selection are controlled, so that the working efficiency of equipment is improved, and the operation cost is reduced.

Description

A kind of double jet type jetting deashing device
Technical field
The utility model belongs to winding-up cleaner technical field, particularly a kind of double jet type jetting deashing device.
Background technology
At present, at chemical industry, oil, the industries such as metallurgy often produce high-temperature dusty gas, because different process need to carry out dedusting to high-temperature dusty gas, realize gas solid separation and gas purification, what often use is to be filtered and realized gas solid separation by the filter core in deduster, dusty gas through filtration, purification enters air-purifying chamber, dust-filtering is stayed in the dirt pocket of deduster, be deposited in ash bucket, and the filter core that deduster is used its outer surface in dust removal by filtration process can adsorb a large amount of granule dusts, along with dust constantly increases, will affect filter quality, therefore need the dust that cartridge surface is piled up to remove, what generally use now is that injection tube realizes reverse deashing, but the result of blowback must be to make the air having purified again enter the space before purification, because the purified gas scale of construction of each winding-up use is larger, secondary filter could purify again, be unfavorable for increasing work efficiency, and need to increase gas boosting equipment.In addition while winding-up due to tubulose spout, can only clear up winding-up mouthful corresponding filter core part, spout can not change blowback direction, and have not easy cleaning of deashing dead angle in winding-up process, the solid all the more difficulty of unfavorable accumulation meeting of jetting is removed, therefore well thoroughly deashing dedusting; Also there is the design of part producer to adopt dust removal with machine device, as manipulator front end is installed brush, or mechanical oscillation method, but not only complex structure, and because action consistency is poor, easily damage the filter core of deduster, the air-purifying chamber that after filter core damage, dust enters deduster will removing pollutant gas be brought subsequent handling into and is caused great loss.Therefore, need badly and solve the problems referred to above making further improvement and bring new ideas aspect filter core dedusting.
Utility model content
The utility model object is to solve the problems of the technologies described above, provide a kind of with low cost, can fast dust-removing, double jet type jetting deashing device that ash-removal effect is good.
For achieving the above object, the technical solution adopted in the utility model is: a kind of double jet type jetting deashing device, it comprises two-way blowing gas carrier pipe and injection tube, wherein a road blowing gas carrier pipe connects the top nozzle of the filter core top that is positioned at deduster, an other road blowing gas carrier pipe is connected in the lower nozzle of the filter core below of deduster, for the blowing gas carrier pipe of described lower nozzle air feed connects deduster dusty gas admission line, for the blowing gas carrier pipe of described top nozzle air feed connects dust catcher gas purifying chamber escape pipe or external feeder.
Described blowing gas carrier pipe is provided with pressure-raising device and heater.
Described top nozzle and lower nozzle inlet end arrange electromagnetic impulse valve.
Described top nozzle inserts described filter core or covers described filter core top by Venturi tube.
Described lower nozzle comprises some injector heads unit, and described injector head cell distribution is in all sides of described filter core.
Outlet side, described injector head unit cross sectional shape is circular-arc or fan-shaped.
Described injector head unit strings is connected to Venturi tube accelerator.
Described blowing gas carrier pipe is entering deduster position set temperature checkout gear, and described temperature-detecting device connects described heater.
Described heater is electric heater or burner.
A kind of double jet type jetting deashing technique, in described blowing gas carrier pipe, temperature is controlled at 350~750 DEG C, internal pressure is controlled at 0.5~2.5MP, described two-way blowing gas carrier pipe alternate blowing, described top nozzle winding-up number of times: described lower nozzle winding-up number of times is 1:0.5~4.
Further, in described blowing gas carrier pipe, temperature is controlled at 480~650 DEG C.
The utility model comprises two-way blowing gas carrier pipe and injection tube, wherein lead up to top nozzle blowback, can utilize gases at high pressure to expand and blow dust stratification open, an other road utilizes lower nozzle winding-up, the ingenious up big and down small tapered pole body structure feature of utilizing described filter core, the air-flow of ejection gas moves along filter core outer wall, has and well peels off effect, can realize preferably the object that the dust stratification of filter core outside is removed; There is good ash-removal effect; For the blowing gas carrier pipe of described lower nozzle air feed connects deduster dusty gas admission line, can utilize dusty gas jetting and carrying out ash disposal at a high speed, source of the gas carrys out Self-duster dusty gas admission line, itself there is higher temperature, can reduce greatly the cost to winding-up gas heating, pressurization, there is good economic benefit, and the dust granules in the dusty gas of accelerated motion has good shot-peening effect, pulverize, loosening dust horizon effect is good, and winding-up process remains the process of a filtration, is convenient to fast dust-removing; Described blowing gas carrier pipe is provided with pressure-raising device and heater, is adapted to the working environment of HTHP, can ensure the temperature of blowing gas, avoids the low condensation that affects coal tar wet goods composition in dusty gas of blowing gas temperature and damage equipment; Described top nozzle inserts described filter core or covers described filter core top by Venturi tube, and the former needs multiple nozzles to be connected respectively in injection tube, and the latter can once cover some filter cores, realizes the once dedusting of multiple filter cores; Described lower nozzle comprises some injector heads unit, described injector head cell distribution is in all sides of described filter core, described in described nozzle, outlet side, injector head unit cross sectional shape is circular-arc or fan-shaped, the form of the little outlet of multiple spot, a common powerful winding-up air ring, the gas stripping good dedusting effect of forming; Described injector head unit strings is connected to Venturi tube accelerator, has good secondary pressurized effect, is convenient to improve injecting velocity; Described blowing gas carrier pipe is entering deduster position set temperature checkout gear, and described temperature-detecting device connects described heater.
The utility model modern design is ingenious, adopt in filter element of duster and spray outside blowback and bottom and spray and peel off the purge mode combining, and control winding-up temperature and injection method selection, spray reverse gas cleaning mode in tradition has been carried out to innovation design, draw rational temperature and pressure values according to design and experiment, ensure the good gasification result of coal tar wet goods composition, avoid condensation, and provide the operating type of described two-way blowing gas carrier pipe alternate blowing, concrete, described top nozzle winding-up number of times: described lower nozzle winding-up number of times is 1:0.5~4, not only avoid the not thorough and Dead Core Problems of independent blowback, also reduce single dusty gas winding-up and cause the blockage problem in outer some hole of filter core, the two ingenious combination, alternately operating, well realize the effect that Ring divests dirt and reverse gas cleaning, dedusting is more thorough, not only take full advantage of the gas source temperature heat of dusty gas, and effectively reduce Purge gas secondary and enter that the equipment operating efficiency that causes in the dirt pocket of deduster reduces and cost increase.The utility model is reasonable in design, with low cost, and device security is reliable, the cycle of operation is long, the efficiency of dust collection of filter core has improved more than 5%, and operating cost reduces more than 6%, has good economic benefit, start new approach for filter core dedusting aspect, had good value for applications.
brief description of the drawings
Below in conjunction with accompanying drawing, the utility model is further detailed:
Fig. 1 is a kind of structural representation of the present utility model;
Fig. 2 is a kind of structural representation of nozzle segment under the utility model;
Fig. 3 is the another kind of structural representation of the utility model top nozzle part;
Fig. 4 is the another kind of structural representation of the utility model injection unit.
Detailed description of the invention
Embodiment mono-
As shown in Figure 1 and Figure 2, a kind of double jet type jetting deashing device, it comprises two-way blowing gas carrier pipe 1 and injection tube 2, wherein a road blowing gas carrier pipe 1 connects the top nozzle 4 of filter core 3 tops that are positioned at deduster, an other road blowing gas carrier pipe 1 is connected in the lower nozzle 5 of filter core 3 belows of deduster, for the blowing gas carrier pipe 1 of described lower nozzle 5 air feed connects deduster dusty gas admission line 6, for the blowing gas carrier pipe 1 of described top nozzle 4 air feed connects dust catcher gas purifying chamber escape pipe or external feeder.
Described blowing gas carrier pipe 1 is provided with pressure-raising device 7 and heater 8.
Described top nozzle 4 and lower nozzle 5 inlet ends arrange electromagnetic impulse valve 9.
Described top nozzle 4 inserts described filter core 3.
Described lower nozzle 5 comprises some injector heads unit 10, and described injector head unit 10 is distributed in all sides of described filter core 3.
Described injector head unit 10 outlet side cross sectional shapes are circular-arc.
Described injector head unit 10 is serially connected with Venturi tube accelerator 11.
Described blowing gas carrier pipe 1 is entering deduster position set temperature checkout gear 12, and described temperature-detecting device 12 connects described heater 8, and described heater 8 is electric heater.
A kind of double jet type jetting deashing technique, the interior temperature of described blowing gas carrier pipe 1 is controlled at 350~750 DEG C, internal pressure is controlled at 0.5~2.5MP, described two-way blowing gas carrier pipe 1 alternate blowing, described top nozzle 4 number of times of jetting: described lower nozzle 5 number of times of jetting is 1:0.5~4.
Embodiment bis-
As shown in Figure 1,3, be with the difference of embodiment mono-: described top nozzle 4 covers described filter core 3 tops by Venturi tube 13.
Embodiment tri-
As shown in Figure 4, be with the difference of embodiment mono-: described injector head unit 10 outlet side cross sectional shapes are fan-shaped.
Embodiment tetra-
Be with the difference of embodiment mono-or two: described heater 8 is burner.
Embodiment five
Be with the difference of arbitrary described embodiment in embodiment mono-~tetra-: the interior temperature of described blowing gas carrier pipe 1 is controlled at 480~650 DEG C.
The utility model comprises two-way blowing gas carrier pipe and injection tube, wherein lead up to top nozzle blowback, can utilize gases at high pressure to expand and blow dust stratification open, an other road utilizes lower nozzle winding-up, the ingenious up big and down small tapered pole body structure feature of utilizing described filter core, the air-flow of ejection gas moves along filter core outer wall, has and well peels off effect, can realize preferably the object that the dust stratification of filter core outside is removed; There is good ash-removal effect; For the blowing gas carrier pipe of described lower nozzle air feed connects deduster dusty gas admission line, can utilize dusty gas jetting and carrying out ash disposal at a high speed, source of the gas carrys out Self-duster dusty gas admission line, itself there is higher temperature, can reduce greatly the cost to winding-up gas heating, pressurization, there is good economic benefit, and the dust granules in the dusty gas of accelerated motion has good shot-peening effect, pulverize, loosening dust horizon effect is good, and winding-up process remains the process of a filtration, is convenient to fast dust-removing; Described blowing gas carrier pipe is provided with pressure-raising device and heater, is adapted to the working environment of HTHP, can ensure the temperature of blowing gas, avoids the low condensation that affects coal tar wet goods composition in dusty gas of blowing gas temperature and damage equipment; Described top nozzle inserts described filter core or covers described filter core top by Venturi tube, and the former needs multiple nozzles to be connected respectively in injection tube, and the latter can once cover some filter cores, realizes the once dedusting of multiple filter cores; Described lower nozzle comprises some injector heads unit, described injector head cell distribution is in all sides of described filter core, described in described nozzle, outlet side, injector head unit cross sectional shape is circular-arc or fan-shaped, the form of the little outlet of multiple spot, a common powerful winding-up air ring, the gas stripping good dedusting effect of forming; Described injector head unit strings is connected to Venturi tube accelerator, has good secondary pressurized effect, is convenient to improve injecting velocity; Described blowing gas carrier pipe is entering deduster position set temperature checkout gear, and described temperature-detecting device connects described heater.
The utility model modern design is ingenious, adopt in filter element of duster and spray outside blowback and bottom and spray and peel off the purge mode combining, and control winding-up temperature and injection method selection, spray reverse gas cleaning mode in tradition has been carried out to innovation design, draw rational temperature and pressure values according to design and experiment, ensure the good gasification result of coal tar wet goods composition, avoid condensation, and provide the operating type of described two-way blowing gas carrier pipe alternate blowing, concrete, described top nozzle winding-up number of times: described lower nozzle winding-up number of times is 1:0.5~4, not only avoid the not thorough and Dead Core Problems of independent blowback, also reduce single dusty gas winding-up and cause the blockage problem in outer some hole of filter core, the two ingenious combination, alternately operating, well realize the effect that Ring divests dirt and reverse gas cleaning, dedusting is more thorough, not only take full advantage of the gas source temperature heat of dusty gas, and the equipment operating efficiency of effectively avoiding Purge gas secondary to enter causing in the dirt pocket of deduster reduces and cost increase.The utility model is reasonable in design, with low cost, and device security is reliable, the cycle of operation is long, the efficiency of dust collection of filter core has improved more than 5%, and operating cost reduces more than 6%, has good economic benefit, start new approach for filter core dedusting aspect, had good value for applications.

Claims (8)

1. a double jet type jetting deashing device, it is characterized in that: it comprises two-way blowing gas carrier pipe and injection tube, wherein a road blowing gas carrier pipe connects the top nozzle of the filter core top that is positioned at deduster, an other road blowing gas carrier pipe is connected in the lower nozzle of the filter core below of deduster, for the blowing gas carrier pipe of described lower nozzle air feed connects deduster dusty gas admission line, for the blowing gas carrier pipe of described top nozzle air feed connects dust catcher gas purifying chamber escape pipe or external feeder.
2. double jet type jetting deashing device as claimed in claim 1, is characterized in that: described blowing gas carrier pipe is provided with pressure-raising device and heater.
3. double jet type jetting deashing device as claimed in claim 1, is characterized in that: described top nozzle and lower nozzle inlet end arrange electromagnetic impulse valve.
4. double jet type jetting deashing device as claimed in claim 1, is characterized in that: described top nozzle inserts described filter core or covers described filter core top by Venturi tube.
5. double jet type jetting deashing device as claimed in claim 1, is characterized in that: described lower nozzle comprises some injector heads unit, described injector head cell distribution is in all sides of described filter core.
6. double jet type jetting deashing device as claimed in claim 5, is characterized in that: outlet side, described injector head unit cross sectional shape is circular-arc or fan-shaped.
7. double jet type jetting deashing device as described in claim 5 or 6, is characterized in that: described injector head unit strings is connected to Venturi tube accelerator.
8. double jet type jetting deashing device as claimed in claim 1, it is characterized in that: described blowing gas carrier pipe is entering deduster position set temperature checkout gear, described temperature-detecting device connects described heater, and described heater is electric heater or burner.
CN201420260979.1U 2014-05-21 2014-05-21 Twin-jet spraying-flushing dust-cleaning device Active CN203874588U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420260979.1U CN203874588U (en) 2014-05-21 2014-05-21 Twin-jet spraying-flushing dust-cleaning device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420260979.1U CN203874588U (en) 2014-05-21 2014-05-21 Twin-jet spraying-flushing dust-cleaning device

Publications (1)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103990331A (en) * 2014-05-21 2014-08-20 河南龙成煤高效技术应用有限公司 Dual-injection type injecting and dust-removing device and process

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103990331A (en) * 2014-05-21 2014-08-20 河南龙成煤高效技术应用有限公司 Dual-injection type injecting and dust-removing device and process
CN103990331B (en) * 2014-05-21 2016-08-24 河南龙成煤高效技术应用有限公司 A kind of double jet type jetting deashing device and technique thereof

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