CN1049366C - Accelerated impact dust remover of granite and its making method - Google Patents
Accelerated impact dust remover of granite and its making method Download PDFInfo
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- CN1049366C CN1049366C CN96108313A CN96108313A CN1049366C CN 1049366 C CN1049366 C CN 1049366C CN 96108313 A CN96108313 A CN 96108313A CN 96108313 A CN96108313 A CN 96108313A CN 1049366 C CN1049366 C CN 1049366C
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- chamber
- granite
- accelerated impact
- dust
- dust remover
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Abstract
The present invention relates to an accelerated impact dust remover of granite and a manufacturing method thereof. The accelerated impact dust remover of granite comprises a gas intake connection tube, a centrifugal purification chamber with 2 symmetrical S-shaped sections, a dust collecting and water sealing chamber, a water replenishing and balancing bucket communicated with the dust collecting and water sealing chamber, a blowoff valve, a gas-liquid separation chamber in which multilayer water baffles are arranged, a gas collecting chamber, a gas out connection tube, a base and an accelerated impact chamber whose section is in the shape of a reverse horn. Most of members of the accelerated impact dust remover of granite are made of natural granite and are glued by mortar. The present invention has the following advantages that dust removing efficiency is larger than 97% and SO2 removing rate is higher than 50% indicated by tests, and the present invention has the characteristics of no secondary pollution, small equipment volume, small occupation of land, large treating capacity, convenient operation and management, less water consumption, corrosion resistance, wear resistance, long service life, etc.
Description
The cleaner that the present invention relates to a kind of ash-laden gas is accelerated impact dust remover of granite and preparation method thereof.
In the 331st page of in August, 1984 China Construction Industry Press " industrial ventilation dedusting technology " Roto-clone type self-induced scrubber and in November, 1985 Shanghai science tech publishing house the Chemical Equipment Design pandect in disintegrating scrubber CCJ/A type dedusting unit in " cleaner design " the 375th page, after its dust-contained airflow enters body, air velocity all is to reduce greatly to flow downward, separate oarse-grained grit in the hope of grit by the gravitational settling effect, its efficiency of dust collection is low, especially in the air-flow in, short grained grit is failed sedimentation separation and is increased the weight of the load of back dedusting.Simultaneously, air-flow is more steady flowing of this interval, can not intensify water body, and no water smoke produces, and can't play the effect that water smoke is caught dirt.And above-mentioned dirt deduster is steel or the manufacturing of common metal material, and it is big not to be suitable for corrosivity, and the big gas purification of wearing and tearing especially is not suitable for the purified treatment of boiler smoke.
Originally the objective of the invention is to provide a kind of accelerated impact dust remover of granite of good dedusting effect, and a kind of preparation method of corrosion-resistant, anti abrasive above-mentioned accelerated impact dust remover of granite is provided.
For reaching above-mentioned purpose, the present invention has adopted the part-structure in Roto-clone type self-induced scrubber and the CCJ/A type dedusting unit and has formed through transformation, it comprises air inlet tube, the cross section of two symmetries is the centrifugal clarification chamber of " S " type, liquid level is sealed the control of dust water tight compartment of bottom, centrifugal clarification chamber and is communicated with the moisturizing balance bucket of control of dust water tight compartment, blowoff valve, in also comprising, it establishes the gas-liquid separation chamber of multilayer water fender, collection chamber, outgoing gas connection tube, base is characterized in that: it also is provided with, and top is communicated with air inlet tube, the bottom is communicated with the thereunder symmetrical centrifugal clarification of setting chamber, under be control of dust water tight compartment liquid level, the cross section gradually closing is for being inverted flaring accelerated impact chamber.The bottom of accelerated impact chamber is the acceleration throat that the both sides rectangular or cross section, cross section are circular arc, and its degree of depth is the 100-300 millimeter.The preparation method of above-mentioned deduster is, removes air inlet tube, outgoing gas connection tube, and outside the blowoff valve, all members all adopt the natural granite processing and fabricating to form, and member connects with anticorrosion, wear-resisting epoxy glue earth rubber and is assembled into integral body.
The present invention compared with prior art has following advantage: by test shows, its efficiency of dust collection is greater than 97%, SO
2Clearance is higher than 50%, and does not produce secondary pollution, and equipment volume is little, takes up an area of to lack, and treating capacity is big, convenient operation and management, and water consumption is few, and is corrosion-resistant, wear-resistant, characteristics such as long service life.
Accompanying drawing is a structural representation of the present invention.
Below in conjunction with accompanying drawing invention is described in further detail: as shown in the figure, it is by air inlet tube (1), and accelerated impact chamber (2) quicken throat (3), symmetry serpentine centrifugal clarification chamber (4), gas-liquid separation chamber (5), collection chamber (6), outgoing gas connection tube (7), control of dust water tight compartment (8), moisturizing balance bucket (9) blowoff valve (10), pedestal (11), multilayer water fender (12) is formed.
When the present invention uses, ash-laden gas at first enters accelerated impact chamber (2) by air inlet tube (1), and dust-contained airflow is in this district, because of the down washing of the minimizing gradually speed increase in the cross section of flowing through, when air-flow enters acceleration throat (3), then reach the impulse air velocity (10-20m/s) of design.Grit in the air-flow is in downward impulse process, because the continuing to increase of air velocity, its strength of dashing is down also inclined to increasing, makes it to pour effectively in the water body of control of dust water tight compartment (8) and is captured, and has improved the efficiency of dust collection of equipment.
Acceleration air-flow through throat (3), its grit pour in control of dust water tight compartment (8) water body under gravity and action of inertia, and the dirt of most of larger particles and flow separation intensify the water surface simultaneously, form the water smoke space of certain altitude and density.By the air-flow behind the first class purification with after the water droplet of atomizing contacts, divide two strands of mixed airflows that also flow to enter the serpentine centrifugal clarification chamber (4) of left and right symmetry respectively, porch at " S " passage, air velocity was once quickened again, and fully contact with highdensity water smoke, make that more tiny grit is wetting in the air-flow increases the weight of, under action of centrifugal force, grit after the weightening finish is got rid of to the body serpentine passage smooth wall of chamber, the cohesion back flows into water body with water, reach and remove tiny grit, the effect of purifying gas flow once more.
The air-flow that is flowed out by serpentine centrifugal clarification chamber (4) promptly enters gas-liquid separation chamber (5), because of the cross section sudden enlargement, air velocity is reduced suddenly greatly, water droplet in the air-flow is under the gravity effect and sedimentation breaks away from air-flow, air-flow after the dehydration moves upward, contact with multilayer water fender (12), the water droplet in the separation bubble is controlled at below 6% the air-flow moisture content and discharges by collection chamber (6), outgoing gas connection tube (7) more once again.
Keep certain water level in the control of dust water tight compartment (8), the height of water level is definite when the operation debugging, but need seal the bottom of centrifugal clarification chamber (4).Be deposited in the taper bucket after the grit that is captured by accelerated impact and " S " centrifugal clarification chamber (4) falls into control of dust water tight compartment (8) water body, be in operation and discharge in dust-precipitator by blowoff valve (10) aperiodically.
Moisturizing balance bucket (9) is folded water amount in the water yield of replenishing high-temperature flue gas and being evaporated and the dust discharge mud, and water seal circle is controlled in the scope of design in the retainer, to guarantee dedusting and to slough SO
2Effect.
Above-mentioned member removes air inlet tube (1), and outgoing gas connection tube (7) outside the blowoff valve (10), all adopts the natural granite processing and fabricating to form, and member connects with anticorrosion, wear-resisting epoxy glue earth rubber and is assembled into integral body.
Claims (3)
1, a kind of accelerated impact dust remover of granite, it comprises air inlet tube, the cross section of two symmetries is the centrifugal clarification chamber of " S " type, liquid level is sealed the control of dust water tight compartment of bottom, centrifugal clarification chamber and is communicated with the moisturizing balance bucket of control of dust water tight compartment, blowoff valve, in also comprising, it establishes the gas-liquid separation chamber of multilayer water fender, collection chamber, outgoing gas connection tube, base is characterized in that: it also is provided with, and top is communicated with air inlet tube, the bottom be provided with that left-right symmetry " S " type centrifugal clarification chamber thereunder is communicated with, under be control of dust water tight compartment liquid level, the cross section is for being inverted flaring accelerated impact chamber.
2, accelerated impact dust remover of granite according to claim 1 is characterized in that: the bottom of accelerated impact chamber is the acceleration throat that the both sides rectangular or cross section, cross section are circular arc, and its degree of depth is the 100-300 millimeter.
3, accelerated impact dust remover of granite according to claim 1 and 2 is characterized in that: the air velocity of quickening the throat place is 10-20M/S.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96108313A CN1049366C (en) | 1995-12-08 | 1996-06-19 | Accelerated impact dust remover of granite and its making method |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN95118961.1 | 1995-12-08 | ||
| CN95118961 | 1995-12-08 | ||
| CN96108313A CN1049366C (en) | 1995-12-08 | 1996-06-19 | Accelerated impact dust remover of granite and its making method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1149503A CN1149503A (en) | 1997-05-14 |
| CN1049366C true CN1049366C (en) | 2000-02-16 |
Family
ID=25743801
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN96108313A Expired - Fee Related CN1049366C (en) | 1995-12-08 | 1996-06-19 | Accelerated impact dust remover of granite and its making method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1049366C (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103203147B (en) * | 2013-05-02 | 2014-12-17 | 东北大学 | Spraying water storage impact type internal circulating dust remover and dust removal method |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2156927Y (en) * | 1993-05-24 | 1994-02-23 | 刘斌 | Gas induction dust-collector |
-
1996
- 1996-06-19 CN CN96108313A patent/CN1049366C/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2156927Y (en) * | 1993-05-24 | 1994-02-23 | 刘斌 | Gas induction dust-collector |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1149503A (en) | 1997-05-14 |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |