CN205073867U - But efflux smoking control dirt, waste gas vortex purify integrated system - Google Patents
But efflux smoking control dirt, waste gas vortex purify integrated system Download PDFInfo
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- CN205073867U CN205073867U CN201520810211.1U CN201520810211U CN205073867U CN 205073867 U CN205073867 U CN 205073867U CN 201520810211 U CN201520810211 U CN 201520810211U CN 205073867 U CN205073867 U CN 205073867U
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- dust
- waste gas
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- cylindrical shell
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
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- Filtering Of Dispersed Particles In Gases (AREA)
- Treating Waste Gases (AREA)
Abstract
The utility model relates to a to but efflux smoking control dirt, waste gas vortex purify integrated system, utilize decontaminating agent atomizing device with the gas -liquid intensive mixing, make large granule thing in the smoke and dust waste gas, nitrogen oxide, sulphide etc. Obtain diluting, it adsorbs to carry out the micronic dust again, porous structure that steel tendon structure in the device and active carbon rubble are formed plays the effect of aqueous vapor collection to carbon particulate, tar, heavy metal adsorption the time. It includes at least one barrel, has into mouth, outlet flue on the barrel, has at least one whirlwind motor on the barrel, and barrel upper portion sprays the pipeline. Be fixed with a plurality of steel tendons on every motor extension output shaft in the barrel, be fixed with a plurality of steel tendons on the barrel inner wall. Adopt rotatory steel tendon, simple structure, reasonable, reinforcing gas -liquid mixture effect is equipped with the liquid medicine, uses same device to solve dust removal, desulfurization, denitration, improves gas -liquid atomization effect, has improved purification efficiency.
Description
technical field
The utility model relates to the controlled flue dust of a kind of jet, waste gas vortex purification integrated system, utilize cleanser atomising device gas-liquid fully to be mixed, bulky grain thing, nitrogen oxide, sulfide etc. in smoke exhaust are diluted, carry out micronic dust absorption again, the loose structure of the steel tendon structure and activity charcoal rubble composition in device is to the effect playing aqueous vapor collection while carbon particulate, tar, heavy metal adsorption.
Background technology
In the prior art, at present, the operating cost of the technology such as the dry dust removal (comprising bag-type dust and electrostatic precipitation) of smoke exhaust process field is expensive, the situation drier to higher dust of furnace temperature such as circulating sulfuration pool furnaces still can, but be difficult to overcome that grate firing boiler furnace temperature is low, dust humidity great Yi blocks up, increase the problem of smoke evacuation resistance, and system for desulfuration and denitration capturing efficiency supporting is with it lower, operating cost is high; Although and wet dust removal operating cost is low, efficiency is also had a greatly reduced quality.Dry dust removal complex structure, operating cost are high, wet dust removal inefficiency, can not solve the problem of carbon particulate, tar, heavy metal escape.Conventional also has cyclone dust collectors, and comprise cylindrical shell, cylindrical shell has into mouth, outlet flue, cylindrical shell has whirlwind motor, spray pipeline is arranged at cylindrical shell top, and shortcoming is that unreasonable structure, dust removing effects are bad.
Utility model content
The purpose of this utility model be provide for above-mentioned deficiency a kind of structure more rationally, the controlled flue dust of the better jet of dust removing effects, waste gas vortex purification integrated system.Can also accuracy controlling jet.
Technical solution of the present utility model is: the controlled flue dust of jet, waste gas vortex purification integrated system, comprise at least one cylindrical shell (one or more levels dedusting), cylindrical shell have into mouth, outlet flue, cylindrical shell there is at least one motor (motor is many can improve atomizing effect), spray pipeline (add different liquid, can realize dedusting, desulphurization and denitration etc.) is arranged at cylindrical shell top.In cylindrical shell, each motor prolongation output shaft is fixed with multiple steel tendon (or claiming wire bundle, as rice transplanting bunch seedling shape), decontaminant liquid is drenched on the steel tendon of extending shaft, and decontaminant liquid is formed jet by the steel tendon of rotation.Cylinder inboard wall is fixed with multiple steel tendon, in order to catch dirt particle that is that jet hits or barrel bounce-back.Said structure is referred to as cleanser atomising device.Accuracy controlling jet can be realized by control spray pipeline pump motor, whirlwind motor speed.
In such scheme:
Motor prolongation output shaft is fixed with multiple spiral-distributed steel tendon vertically (helical arrangement can improve atomizing effect).Formed " helical axis ".
Cylinder inboard wall is fixed with multiple steel tendon (realizing atomization evenly, without dead angle) of helically arranging along barrel.
Motor is spaced apart three motors, and (motor is many can improve atomizing effect to be optimized for Triangle-Profile.Mutually rub with the hands under the centrifugal action of three rotating shafts and lay abundant atomization).
At least one outlet flue is connected with micronic dust adsorbent equipment, micronic dust adsorbent equipment comprises cavity, cavity upper end closed, lower termination taper control of dust funnel, bell mouth stretches into sedimentation basin water-stop cavity to have into mouth, outlet flue, suspention multiple micronic dust absorption string bag in cavity, the in-built rubble of the string bag, active carbon are a kind of or combine.
String bag outer surface is fixed with multiple steel tendon.
Cylindrical shell basis is concave character type sedimentation basin, and character cut in bas-relief inwall comparatively outer wall is low, for laying filter screen.
Cleanser atomising device and micronic dust adsorbent equipment can be used alone, combinationally use.Or obsolete equipment need not be removed, just can reach ideal effect by technological transformation, because this device does not increase exhaust resistance.Cleanser atomising device main body cylinder shape cavity, upper end sealing, under connect conical funnel, bell mouth stretches into sedimentation basin with water-stop.There are import and export the side, two ends up and down of main body cylinder shape, the direction imported and exported and the circumscribed line parallel of body cylindrical, three motors are preferably installed on top, the position of motor is three summits of equilateral triangle, and vertex of a triangle is positioned at body diameter 0.382 place, and three major axis extend to lower body part, three axle heads are three fan leafs, what axle was installed is mild steel tow, and is arranged in helical form, and cylinder-shaped body inwall is by many spiral mild steel tow.Purifying liquid mouth is entered directly to drench by top (to be convenient to form jet) with on the helical axis of steel tendon, mutually rubs with the hands and lay abundant atomization under the centrifugal action of three rotating shafts.Micronic dust adsorbent equipment is that main body upper end closed, lower termination conical hopper, bell mouth stretches into sedimentation basin with water-stop by circular or square cavity.The direction imported and exported and the circumscribed line parallel of body cylindrical, adsorb terminal matrix by micronic dust in main body to form, micronic dust absorption terminal is a strip string bag, string bag outer wall is the steel tendon at ten centimeters of intervals, in-built 5-10cm porous rubble and active carbon and layering are loaded, string bag internal diameter and length design according to treating capacity, and micronic dust absorption terminal is cellular longitudinal arrangement (or rectangular).Basis is concave character type sedimentation basin, and character cut in bas-relief inwall is the low 50cm of outer wall comparatively, for laying filter screen, is separated by cleanser with mud, and filter after-purification liquid and recycle, matrix pond is double does Equipment Foundations.
By the feedback signal of on-line monitoring separately to the dedusting of atomising device, denitration, desulfurization Electric Machine Control, cleanser delivery pump Electric Machine Control, carry out the accurate control of single index.Namely accuracy controlling jet can be realized by control spray pipeline pump motor, whirlwind motor speed (frequency conversion).
The utility model has the advantages that: 1, adopt rotatable wire bundle, simple and reasonable for structure, strengthen gas-liquid mixed effect, be equipped with liquid, use same device to solve dedusting, desulphurization and denitration, improve gas-liquid atomizing effect, improve purification efficiency.To the seizure of bulky grain thing, nitrogen oxide, oxysulfide, micronic dust adsorbent equipment carries out passive adsorption to for fine particle, tar, micro-harmful substance, and isolation steam, to reach perfect clean-up effect.2, adopt Multistage purifying agent atomising device, while flue dust is diluted further, dissolved dilution is carried out to sulfide, again carry out micronic dust absorption and aqueous vapor collection.Reduce cost of investment to a great extent, improve efficiency of dust collection.3, micronic dust adsorbent equipment is equipped with, the loose structure of the steel tendon structure and activity charcoal rubble composition in device is to the effect playing aqueous vapor collection while carbon particulate, tar, heavy metal adsorption, effectively solve the collection of micronic dust, tar, aqueous vapor, dust removing effects is remarkable.
Below in conjunction with accompanying drawing, embodiment of the present utility model is described in further detail.
Accompanying drawing explanation
Fig. 1 is the utility model structure diagram.
Fig. 2 is micronic dust adsorbent equipment structure diagram.
Fig. 3 is embodiment 1 structure diagram.
Fig. 4 is embodiment 2 structure diagram.
Fig. 5 is embodiment 3 structure diagram.
Detailed description of the invention
See Fig. 1-5, parts title is as follows: cylindrical shell 1, enters mouth 2, outlet flue 3, motor 4, output shaft 5, steel tendon 6, micronic dust adsorbent equipment 7, cavity 8, the string bag 9, fan leaf 10, cleanser atomising device 11, base 12, screen pack 13, spray pipeline 14.
See Fig. 1, the controlled flue dust of jet, waste gas vortex purification integrated system, comprises a cylindrical shell 1, cylindrical shell 1 have into mouth 2, outlet flue 3, cylindrical shell 1 has three spaced apart whirlwind motors, 4, three long output shafts 5 extend to lower body part, three output shaft 5 ends are three fan leafs 10.Spray pipeline 14 is arranged at cylindrical shell 1 top.In cylindrical shell 1, each motor prolongation output shaft 5 is fixed with spiral-distributed steel tendon 6(vertically soft or flexible.Only on an output shaft, drawn steel tendon 6 in Fig. 1, other omits), cylindrical shell 1 inwall is also fixed with multiple steel tendon 6 of helically arranging along barrel.Base 12 basis is concave character type sedimentation basin, and character cut in bas-relief inwall is the low 50cm of outer wall comparatively, for laying screen pack 13, is separated by cleanser with mud, and filter after-purification liquid and recycle, matrix pond is double does Equipment Foundations.Steel tendon 6 shape, size, material are not limit, and can be steel wires, also can be other wires; Can be tufted, multiple, also can be single; Can be straight, also can be bending.
See Fig. 2, micronic dust adsorbent equipment 7 comprises cavity 8, cavity 8 upper end closed, lower termination taper control of dust funnel, cavity 8 has into mouth 2, outlet flue 3, suspention multiple micronic dust absorption string bag 9 in cavity 8, the in-built rubble of the string bag 9, active carbon are a kind of or combine, the string bag 9 outer surface is fixed with in multiple steel tendon 6(Fig. 2 and only on a string bag, has drawn steel tendon 6, rubble, active carbon, and other omits).
See Fig. 3, can be that a cleanser atomising device 11 is alone, also can be that multiple cleanser atomising device 11 combines use, also can be that one or more cleanser atomising device 11 combinationally uses with micronic dust adsorbent equipment 7.Different group cleanser atomising device 11 can spray different dedusting liquid as required.Fig. 3 is one is that cleanser atomising device 11 and a micronic dust adsorbent equipment 7 combinationally use.
See Fig. 4, be that three cleanser atomising devices 11 are connected use, then combinationally use with a micronic dust adsorbent equipment 7.
See Fig. 5, be two groups of cleanser atomising devices 11, often organize three cleanser atomising devices 11 and to connect use, then combinationally use with a micronic dust adsorbent equipment 7.
Operation principle: see Fig. 1-5, spray pipeline 14 purifying liquid mouth is entered by top and directly drenches on output shaft 5, mutually rub with the hands under the centrifugal action of three rotating output shafts 5 and lay abundant atomization, when flue gas or waste gas enter form vortex by entering mouth 2 under the effect of three fan leafs 10, decontaminant liquid fully completes the mixing of gas-liquid under the effect of spiral centrifugal simultaneously, and discarded object is delivered to base 12 sedimentation basin through conical hopper by the cleaning solution pooled together.Gas after washing is discharged by outlet flue 3 and is entered in micronic dust adsorbent equipment 7, micronic dust adsorbent equipment 7 is by circular or square cavity 8 upper end closed, lower termination conical hopper, the direction imported and exported and the circumscribed line parallel of body cylindrical, adsorb the string bag 9 matrix by micronic dust in main body to form, the micronic dust absorption string bag 9 is strip string bags, string bag outer wall is the steel tendon 6 at ten centimeters of intervals, in-built 5-10cm porous rubble and active carbon and layering are loaded, the micronic dust absorption string bag 9 is in cellular (or rectangular) longitudinal arrangement, to micronic dust, tar and micro heavy absorption, the string bag 9 internal diameter and length design according to gas treatment amount, base 12 is concave shape sedimentation basin, concave shape inwall is the low 50cm of outer wall comparatively, for laying screen pack 13, cleanser is separated with mud, scavenging solution after filtration recycles, concave shape pond is double does Equipment Foundations, mud is sent by scrapper conveyor.
Describe above, just detailed description of the invention of the present utility model, various illustrating is not construed as limiting flesh and blood of the present utility model.
Claims (7)
1. the controlled flue dust of jet, waste gas vortex purification integrated system, comprise at least one cylindrical shell (1), cylindrical shell (1) have into mouth (2), outlet flue (3), cylindrical shell (1) there is at least one motor (4), spray pipeline is arranged at cylindrical shell (1) top, it is characterized in that, in cylindrical shell (1), each motor prolongation output shaft (5) is fixed with multiple steel tendon (6), cylindrical shell (1) inwall is fixed with multiple steel tendon (6).
2., according to the controlled flue dust of jet according to claim 1, waste gas vortex purification integrated system, it is characterized in that motor extends on output shaft (5) and be fixed with multiple spiral-distributed steel tendon vertically (6).
3., according to the controlled flue dust of the jet described in claim 1 or 2, waste gas vortex purification integrated system, it is characterized in that cylindrical shell (1) inwall being fixed with multiple steel tendon (6) of helically arranging along barrel.
4., according to the controlled flue dust of jet according to claim 3, waste gas vortex purification integrated system, it is characterized in that motor (4) is for spaced apart three motors.
5. according to the controlled flue dust of jet according to claim 4, waste gas vortex purification integrated system, it is characterized in that at least one outlet flue (3) is connected with micronic dust adsorbent equipment (7), micronic dust adsorbent equipment comprises cavity (8), cavity (8) upper end closed, lower termination taper control of dust funnel, cavity (8) has into mouth (2), outlet flue (3), the multiple micronic dust absorption string bag (9) of suspention in cavity (8), the string bag (9) in-built rubble, active carbon are a kind of or combine.
6., according to the controlled flue dust of jet according to claim 5, waste gas vortex purification integrated system, it is characterized in that the string bag (9) outer surface is fixed with multiple steel tendon (6).
7. according to the controlled flue dust of jet according to claim 1, waste gas vortex purification integrated system, it is characterized in that at least one outlet flue is connected with micronic dust adsorbent equipment (7), micronic dust adsorbent equipment comprises cavity (8), cavity (8) upper end closed, lower termination taper control of dust funnel, cavity (8) has into mouth (2), outlet flue (3), the multiple micronic dust absorption string bag (9) of suspention in cavity (8), the string bag (9) in-built rubble, active carbon are a kind of or combine; The string bag (9) outer surface is fixed with multiple steel tendon (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520810211.1U CN205073867U (en) | 2015-10-20 | 2015-10-20 | But efflux smoking control dirt, waste gas vortex purify integrated system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520810211.1U CN205073867U (en) | 2015-10-20 | 2015-10-20 | But efflux smoking control dirt, waste gas vortex purify integrated system |
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| Publication Number | Publication Date |
|---|---|
| CN205073867U true CN205073867U (en) | 2016-03-09 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520810211.1U Withdrawn - After Issue CN205073867U (en) | 2015-10-20 | 2015-10-20 | But efflux smoking control dirt, waste gas vortex purify integrated system |
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| CN (1) | CN205073867U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105233654A (en) * | 2015-10-20 | 2016-01-13 | 戚全有 | Jet flow controllable smoke and waste gas vortex purifying comprehensive system |
| CN106047424A (en) * | 2016-06-30 | 2016-10-26 | 华东理工大学 | Coke oven gas hydrogen sulfide gas recovery method and device |
| CN106237799A (en) * | 2016-09-30 | 2016-12-21 | 江苏绿叶环境工程集团有限公司 | A kind of flue gas desulphurization system |
-
2015
- 2015-10-20 CN CN201520810211.1U patent/CN205073867U/en not_active Withdrawn - After Issue
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105233654A (en) * | 2015-10-20 | 2016-01-13 | 戚全有 | Jet flow controllable smoke and waste gas vortex purifying comprehensive system |
| CN106047424A (en) * | 2016-06-30 | 2016-10-26 | 华东理工大学 | Coke oven gas hydrogen sulfide gas recovery method and device |
| CN106047424B (en) * | 2016-06-30 | 2021-12-10 | 华东理工大学 | Coke oven gas hydrogen sulfide gas recovery method and device |
| CN106237799A (en) * | 2016-09-30 | 2016-12-21 | 江苏绿叶环境工程集团有限公司 | A kind of flue gas desulphurization system |
| CN106237799B (en) * | 2016-09-30 | 2020-02-14 | 江苏绿叶环境工程集团有限公司 | Flue gas desulfurization system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160309 Effective date of abandoning: 20180209 |