CN102580409A - Surface engineering rust removal air purification core separation system - Google Patents
Surface engineering rust removal air purification core separation system Download PDFInfo
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- CN102580409A CN102580409A CN2012100664253A CN201210066425A CN102580409A CN 102580409 A CN102580409 A CN 102580409A CN 2012100664253 A CN2012100664253 A CN 2012100664253A CN 201210066425 A CN201210066425 A CN 201210066425A CN 102580409 A CN102580409 A CN 102580409A
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- cyclone collector
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Abstract
The invention relates to a surface engineering rust removal air purification core separation system which is characterized by comprising a core separator, wherein a gas inlet is formed at the lower end of the side wall of an outer barrel of the core separator; a circulating gas outlet is formed at the upper end of the side wall of the core separator; a separator inner barrel is arranged at the upper end inside the core separator; a clean gas outlet is formed at the outer end of the inner barrel of the separator; the gas inlet is connected with a fan by a pipeline; the circulating gas outlet is connected with a cyclone collector by a pipeline; an ash hopper is arranged at an outlet at the lower end of the cyclone collector; and a gas outlet at the upper end of the cyclone collector is connected with an inlet of the fan by a pipeline. The system is an integrated device invented by combining the reflux friction principle according to the principle of fluid mechanics and rheological mechanics. According to the invention, polluted air with large air flow can be treated, small solid particles, powder and dust (gas with high working humidity) can be effectively separated, no consumable filtering material is arranged inside the surface engineering rust removal air purification core separation system, and the damping ratio is particularly low.
Description
Technical field
The present invention relates to a kind of air cleaning unit, especially a kind of Surface Engineering rust cleaning air cleaning core piece-rate system.
Background technology
Concerning public health, air quality is vital to our breathing.The diffusion of control particle is important society need.Be used for the cost of particle control appliance recent years, accounted for 60% of total Air Pollution Control, is used for the cost of industrial particle DIFFUSION CONTROLLED really, more taller than the summation that is used for whole gas DIFFUSION CONTROLLED.
Treatment of Metal Surface has traditional mechanical-physical derusting process, conventional bead and the mechanical grinding of adopting.When adopting bead and mechanical grinding; Produce a large amount of contaminated airs that contains materials such as oxide, dust, oil, dust, can not directly discharge (because contaminated environment), therefore many must contaminated air the processing; Reach discharge standard, the protection environment.Above air-polluting processing mode generally there are following several kinds of modes both at home and abroad at present: 1, cyclone dust removal; 2, pocket type pulsed dedusting; 3, deposition dedusting; 4, water smoke spraying and dedusting; 5, filter element filtering dedusting etc.The general volume of the air-polluting treating apparatus of tradition is much bigger, is that the air-polluting treating capacity of reason is bigger, and for example: cyclone dust removal must have a lot of platform parallel connections; Sack cleaner besides, volume are very big, and general filter bag (100 * 2 meters) is many about 100, and filter bag is easily-consumed products simultaneously, can not adapt to the higher gas of humidity; The machine volume of deposition dedusting is bigger, and general volume is about 6 ~ 10 cubes; The water smoke spraying and dedusting, volume is more a little bit smaller than the deposition dedusting, but after the water of spray pollutes, must carry out sewage disposal, increases operating cost; The filter element filtering dedusting, volume is same bigger, pollutes especially easily simultaneously, can not adapt to the higher and higher gas of solids content of humidity, and it is higher to change frequency ratio, therefore can only use with other low efficient filter series connection.
Summary of the invention
The objective of the invention is to overcome the deficiency that exists in the prior art, a kind of Surface Engineering rust cleaning air cleaning core piece-rate system is provided, can handle the contaminated air of big air quantity, can effectively separate little solid particle, dust, dust.
According to technical scheme provided by the invention; Said Surface Engineering rust cleaning air cleaning core piece-rate system; It is characterized in that: comprise core separator, the side wall lower ends of said core separator urceolus is provided with gas feed, is provided with the recyclegas outlet in the sidewall upper of said core separator; Inner upper end at core separator is provided with the separator inner core, and the outer end of said separator inner core is the clean air outlet; Said gas feed is connected with blower fan through pipeline, and the recyclegas outlet is connected with cyclone collector through pipeline, and the exit, lower end of cyclone collector is provided with ash bucket, and the gas vent of cyclone collector upper end is connected with the import of blower fan through pipeline.
The present invention is according to the principle of hydrodynamics and rheology; The integration unit of the principle invention that rubs in conjunction with refluxing; The present invention can handle the contaminated air of big air quantity; Can effectively separate little solid particle, dust, dust (adapting to the higher gas of humidity), the inner filtering material that does not have easy consumption, Damping Scale is low especially.Dust removing effects of the present invention can reach 98%.The present invention is higher 4 ~ 6 times than the efficient of cyclone dust collectors the most efficiently.The present invention has broader control range than other centrifugal deduster.Gas temperature of the present invention can reach 800 ℃, and is perhaps higher.Initial cost and operating cost that the present invention is more much lower than other high-efficiency dust remover are 1/3 of electrostatic precipitation, bag-type dustings, are 1/2 of wet dedusting, filter core dedustings, and operating cost, maintenance cost are minimum.The present invention can satisfy requirement newly-built or reconstruction factory.Part that the present invention need not change or parts.The present invention has unique design, and gas circulation can be separated, and can collect again.The present invention can purify the air that Surface Engineering rust cleaning produces, again can be, Lime Factory's shaft kiln dedusting in the cement plant, and smelting furnace, chimney stack, high dust carry out dedusting.
Description of drawings
Fig. 1 is a structural representation of the present invention.
The specific embodiment
Below in conjunction with concrete accompanying drawing the present invention is described further.
As shown in the figure: Surface Engineering rust cleaning air cleaning core piece-rate system comprises core separator 1, cyclone collector 2, ash bucket 3, blower fan 4, separator inner core 5, clean air outlet 6, gas feed 7, recyclegas outlet 8 etc.
The present invention includes core separator 1; The side wall lower ends of said core separator 1 urceolus is provided with gas feed 7; Sidewall upper at said core separator 1 is provided with recyclegas outlet 8; Inner upper end at core separator 1 is provided with separator inner core 5, and the outer end of said separator inner core 5 is clean air outlet 6; Said gas feed 7 is connected with blower fan 4 through pipeline, supplies the power of flue gas recirculation; Recyclegas outlet 8 is connected with cyclone collector 2 through pipeline, and particle is collected by whirlwind; The exit, lower end of cyclone collector 2 is provided with ash bucket 3, and the gas vent of cyclone collector 2 upper ends is connected with the import of blower fan 4 through pipeline.
Blower fan can be replaced by a syringe, can use under hot conditions, and the present invention can have several kinds of variations, and adding is dense by dedusting, and the grit wear intensity is very big, can be connected on the core separator lower current area to blower fan.The research of the present invention through flow pattern and computer simulation experiment have been carried out the research of detailed strictness to the Secondary Flow in the cyclone dust collectors, and Secondary Flow is to cause to return to flow to make the main cause of cyclone dust collectors low performance.And the design of core separator has just in time overcome these limitation.
The flue gas of solids laden thing is through the import of blower fan (or syringe) introducing core separator, because the result of swirling motion, particle is shifted to periphery by the centre, and the gas of cleaning leaves through outlet, carries the particle peripheral flow.Be discharged to cyclone dust collectors, loop back core separator then.Power provides through air-introduced machine.Separation process and solids are collected in various parts and are independently accomplished; The core separator purifying gas flow; And the particle in the scavenge system, if the efficient of core separator is sufficiently high words, particle can not leave system; But circulation again and again all harvests them and removes it up to cyclone collector.In this system, two independently interactions between the parts make this system can obtain higher collection efficiency; Even the effect of gatherer is low; Because the efficient of core separator is high, overall system efficiency can be predicted out also very high, and overall system efficiency is ε; ε=(ε c * ε s)/(1-ε s (1-ε c)), wherein ε, ε s, ε c are respectively the efficient of system, core separator, cyclone collector.Check that this formula demonstrates, even gatherer efficient is low, as long as core separator efficient is high, overall system efficiency also is high.For example: if ε s is 99%, ε c is 30%, and the efficient of system is 96.7%.This phenomenon can make an explanation with another kind of method: for example: if be 99% to certain volume size particles ε s; This will mean at flue gas and leave before deduster is discharged to atmosphere; It will circulate 100 times; This explanation particle is through gatherer 100 times, and Here it is, and their can be by collected reason greatly.
Carry out the comparison of system to several kinds of dedusters, the principal character of each dust pelletizing system is as shown in table 1.
The principal character of table 1 particle control appliance
| Characteristic | The electric power dedusting | Bag type filtering | Whirlwind is collected | Wet type is cleaned | The present invention |
| Efficiency of dust collection | High | High | Low | High | High |
| Bear the ability of high solid concentration | No | No | Have | No | Have |
| Equipment pressure drop | Very low | Medium low | Medium low | Medium low | Medium low |
| Initial cost | Very high | High | Low | High | Medium low |
| Operating cost | High | High | High | Medium height | Low |
| Bear the ability of HTHP | Ability | Can not | Ability | Can not | Ability |
| Space requirement | High | High | Low | Medium | Low |
| Superpressure on fire from explosion is dangerous | Have | Have | No | No | No |
| Special maintenance requirement | Have | Have | No | No | No |
| Produce ozone | Have | No | No | No | No |
| The wastewater treatment requirement | No | No | No | Have | No |
The table of comparisons 1 can see that core piece-rate system of the present invention has many-sided superiority, makes it to use in many-side, and its characteristic comprises:
(1) high collection efficiency, core separator can effective collection thick with thin two kinds of particles;
(2) can bear high temperature: this system can operate in 100 ~ 500 ℃ (260 ~ 540 ℃), and this is that pocket type can not be compared with other deduster.When surpassing 540 ℃ of these special devices, temperature can be used as recirculation;
(3) compact conformation: fundamental system takes up space little, makes it obtain in little space utilizing;
(4) flexible property is high: this equipment is insensitive to solids concentration, and it both can put into vertical, and is perhaps horizontal, but both upper reaches, again can be dirty;
(5) power consumption: equipment pressure drop and power consumption are higher slightly than general cyclone dust collectors;
(6) initial cost is very low: because this system is very simple, so its initial cost is very low, its initial cost compared with the miscellaneous equipment with equal performance will be low a lot.
The particle diameter of the dedusting separation of core piece-rate system of the present invention is 0.5 μ m; When particle diameter greater than 0.5 μ m Total Test efficient 94.7% ~ 98.0%.
Cyclone dust removal, pocket type pulsed dedusting, deposition dedusting, water smoke spraying and dedusting, filter element filtering dedusting etc. also are being that to be lower than 10 microns particle be invalid to kinetic diameter by removing thin soot dust granule.Core separator of the present invention by contrast can be caught the major part of superfine microparticle in the air-flow, promptly is can all catch greater than 2 ~ 3 microns particle.This is equivalent to the electric precipitator of a mid-efficiency.On the other hand, core separator is also keeping the great advantage of mechanical separator, that is: simple, reliable, compact, can control high solid concentration and low relatively initial cost and maintenance cost.
Claims (1)
1. Surface Engineering rust cleaning air cleaning core piece-rate system; It is characterized in that: comprise core separator (1); The side wall lower ends of said core separator (1) urceolus is provided with gas feed (7); Be provided with recyclegas outlet (8) in the sidewall upper of said core separator (1), be provided with separator inner core (5) in the inner upper end of core separator (1), the outer end of said separator inner core (5) is clean air outlet (6); Said gas feed (7) is connected with blower fan (4) through pipeline; Recyclegas outlet (8) is connected with cyclone collector (2) through pipeline; The exit, lower end of cyclone collector (2) is provided with ash bucket (3), and the gas vent of cyclone collector (2) upper end is connected with the import of blower fan (4) through pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012100664253A CN102580409A (en) | 2012-03-14 | 2012-03-14 | Surface engineering rust removal air purification core separation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012100664253A CN102580409A (en) | 2012-03-14 | 2012-03-14 | Surface engineering rust removal air purification core separation system |
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| Publication Number | Publication Date |
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| CN102580409A true CN102580409A (en) | 2012-07-18 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2012100664253A Pending CN102580409A (en) | 2012-03-14 | 2012-03-14 | Surface engineering rust removal air purification core separation system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105688587A (en) * | 2016-04-15 | 2016-06-22 | 中煤科工集团武汉设计研究院有限公司 | Dust cleaning device for derusting work by sand blasting |
| CN105920925A (en) * | 2016-06-13 | 2016-09-07 | 无锡强工机械工业有限公司 | Air-purifying and core cyclone separation device |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3236031A (en) * | 1963-04-25 | 1966-02-22 | American Air Filter Co | Wet dust separator |
| CN2276113Y (en) * | 1996-04-23 | 1998-03-11 | 潍坊市城区除尘设备制造厂 | Charged core separating dust remover |
| CN202087436U (en) * | 2011-01-04 | 2011-12-28 | 徐州方大环保设备科技有限公司 | Core separating type cyclone dust collector |
| US20120017553A1 (en) * | 2009-03-25 | 2012-01-26 | Hyun Seol Park | Cyclone dust collector |
-
2012
- 2012-03-14 CN CN2012100664253A patent/CN102580409A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3236031A (en) * | 1963-04-25 | 1966-02-22 | American Air Filter Co | Wet dust separator |
| CN2276113Y (en) * | 1996-04-23 | 1998-03-11 | 潍坊市城区除尘设备制造厂 | Charged core separating dust remover |
| US20120017553A1 (en) * | 2009-03-25 | 2012-01-26 | Hyun Seol Park | Cyclone dust collector |
| CN202087436U (en) * | 2011-01-04 | 2011-12-28 | 徐州方大环保设备科技有限公司 | Core separating type cyclone dust collector |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105688587A (en) * | 2016-04-15 | 2016-06-22 | 中煤科工集团武汉设计研究院有限公司 | Dust cleaning device for derusting work by sand blasting |
| CN105920925A (en) * | 2016-06-13 | 2016-09-07 | 无锡强工机械工业有限公司 | Air-purifying and core cyclone separation device |
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Application publication date: 20120718 |