CN2278521Y - Double swirl blade dust-remover - Google Patents
Double swirl blade dust-remover Download PDFInfo
- Publication number
- CN2278521Y CN2278521Y CN 96244696 CN96244696U CN2278521Y CN 2278521 Y CN2278521 Y CN 2278521Y CN 96244696 CN96244696 CN 96244696 CN 96244696 U CN96244696 U CN 96244696U CN 2278521 Y CN2278521 Y CN 2278521Y
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- inner core
- flow plate
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Abstract
The utility model relates to a duplex type rotational flow plate dust remover, which has the advantages of simple structure, high dust removing efficiency, and good service performance. The utility model comprises a housing, an exhaust pipe arranged on the housing, an inner cylinder, an air inlet pipe arranged on the inner cylinder, a dust removal rotational flow plate, a water film structure, a bell mouth-shaped fog excitation sleeve, a dehydrated structure, and a fog removal rotational flow plate. The dehydrated structure is composed of more than two groups of ring-shaped baffle plates arranged on the outer wall of a cylinder and the inner wall of the housing with intervals. The inner cylinder and the fog excitation sleeve are arranged in the housing orderly. Ring-shaped fog excitation gaps formed on the inner wall of the fog excitation sleeve and the outer margin of the bottom of the cylinder body of the inner cylinder. The dust removal rotational flow plate and the fog removal plate are respectively arranged in the cylinder body and the exhaust pipe.
Description
The utility model belongs to the combustion product treatment facility, particularly a kind of compound Gas-Rotation-Plate Dust Separator.
For the protection environment for human survival, prevent atmosphere pollution, the flue gas that burning in the industrial processes is produced must purify.The cyclone type dry method dust of commonly using since efficiency of dust collection low, to the gas cleaning weak effect, eliminated by time limit.Extensively adopt various hydrofilters that industrial smoke is purified at present.These dedusters adopt single purification means usually, though it is simple in structure, but not only dust removing effects is poor, and purified gas is taken water electrode for serious, cause heavy corrosion with blower fan and chimney, although adopt multiple dehydration means, but still have repeatly because of stopping up and resistance increases the situation that the equipment that influences runs well and takes place.
The purpose of this utility model provides a kind of simple in structure, efficiency of dust collection is high, serviceability is good compound Gas-Rotation-Plate Dust Separator.
The utility model is made up of shell, inner core, dedusting eddy flow plate, moisture film structure, sharp mist cover, dehydrated structure and demist eddy flow plate, and shell is for constituting the hollow housing of closed chamber, and its top is provided with the blast pipe that connects with closed chamber; Inner core is the shell-like cylindrical shell that the top is provided with air inlet pipe, and inner core places in the closed chamber of shell, constitutes the dehydration ring cavity between the inwall of its cylindrical shell periphery and shell, and makes its top air inlet pipe pass shell communicating with the external world; The external diameter of dedusting eddy flow plate is corresponding with the inner core cylinder internal diameter, and it places in the cylindrical shell, and is positioned at the joining place of cylindrical shell and air inlet pipe; The moisture film structure has the annular enclosed cover that external diameter is slightly less than the inner core cylinder internal diameter, and its outer wall is all established a plurality of spillway holes and water inlet pipe, and the moisture film structure places in the inner core cylindrical shell and is positioned at the below of dedusting eddy flow plate, and water inlet pipe passes inner core cylindrical shell and shell on it; Swash the mist cover and be bell mouth shape, sharp mist is placed in the closed chamber of shell and is positioned at the inner core below, and makes inner wall surface thereof and inner core cylindrical shell bottom outer rim constitute the sharp mist gap of ring-type; Dehydrated structure is made up of ring baffle plate more than two groups, and annular flap is disposed on inner core cylinder body outer wall and the outer casing inner wall; The external diameter of demist eddy flow plate is corresponding with the blast pipe internal diameter of shell, and places in the blast pipe.
Since the utility model by the shell that is provided with blast pipe, the inner core that is provided with air inlet pipe, dedusting eddy flow plate, moisture film structure, be bell mouth shape and swash the mist cover, be disposed on dehydrated structure and the demist eddy flow plate that the ring baffle plate on cylinder body outer wall and the outer casing inner wall forms more than two groups and form, inner core and sharp mist overlap and place in the shell successively, and outer rim formation ring-type swashs the mist gap bottom the inwall of the sharp mist cover of order and the inner core cylindrical shell; Dedusting eddy flow plate and demist eddy flow plate place respectively in cylindrical shell and the blast pipe.Simple in structure.During use, inject water for dust removal in the enclosure, liquid level is a little less than inner core cylindrical shell bottom surface, and the ring-type that is positioned at inner core and sharp mist cover formation swashs the mist gap location, water inlet pipe through the moisture film structure supplies water to the moisture film structure again, the spillway hole of water on the annular enclosed cover outer wall of moisture film structure flowed out, and form moisture film along the inner core cylinder inboard wall.The air inlet pipe of flue gas through the inner/outer tube top that burning produces enters inner core, through dedusting eddy flow plate it formed to inner rotary flue gas stream, utilizes centrifugal force to isolate major diameter grit in the flue gas and falls into the dedusting water of outer casing underpart, carries out dry dust removal; Rotation flue gas stream contacts with moisture film along the cylinder inboard wall rotation downwards, makes that part grit and sulfur dioxide dissolve in the water in the flue gas, carries out wet dust removal; The rotation flue gas flows to dedusting water liquid level by cylindrical shell and swashs the mist gap location from the ring-type that inner core and sharp mist cover constitutes and go out and evoke water smoke, and the small dust and the sulfur dioxide that rotate in the flue gas dissolve in the water smoke, carry out wet dust removal once more; Purified gas enters and constitutes the dehydration ring cavity between the inwall of cylindrical shell periphery and shell, through dehydrated structure be disposed on more than two groups on cylinder body outer wall and the outer casing inner wall the ring baffle plate baffling upwards, water droplet is separated from Purge gas, dewater; Purge gas after the dehydration rises and enters blast pipe, make it form outside swirling eddy through demist eddy flow plate, utilize centrifugal force to isolate residual droplet and grit in the gas once more, the gas of purification and dehumidification is discharged through air exhauster from the outlet of blast pipe fully, not only efficiency of dust collection height but also serviceability are good, thereby reach the purpose of this utility model.
Fig. 1, be the utility model structural representation profile.
Fig. 2, be that A among Fig. 1 is to view.
Below in conjunction with accompanying drawing the utility model is further elaborated.
As shown in Figure 1, the utility model is made up of shell 1, inner core 2, dedusting eddy flow plate 3, moisture film structure 4, sharp mist cover 5, dehydrated structure 6 and demist eddy flow plate 7, shell 1 is for constituting the hollow housing of closed chamber 11, its top is provided with the blast pipe 12 that connects with closed chamber 11, the port of export of blast pipe is provided with secondary ash chamber 13, and at the upper and lower gas outlet 131 and the ash hole 132 that is connected with air exhauster that be respectively equipped with of secondary ash chamber 13;
The bottom of shell 1 constitutes water storage cavity 14 and the grey chamber 15 that is truncation reverse taper shape successively, is provided with valve 16 between water storage cavity 14 and the grey chamber 15, and the bottom of grey chamber 15 is provided with ash hole 151; Shell 1 periphery is provided with ash position detection architecture 17 and overflow structure 18, ash position detection architecture 17 is made up of ash position plate 171, conduit 172, flexible element 173, guide wheel 174 and weight 175, ash position plate 171 places grey chamber 15 inside top, the straight line portion of conduit 172 is provided with scale, one end of conduit 172 is connected with 15 tops, grey chamber, and connect with grey chamber 15, guide wheel 174 is installed in the other end of conduit 172, one end of flexible element 173 is connected with ash position plate 171, and its other end passes conduit 172, pile warp guide wheel 174 backs are connected with weight 175; Overflow structure 18 is positioned at predetermined level height place.
Inner core 2 is provided with the shell-like cylindrical shell 22 of T-shaped crossing air inlet pipe 21 with it for the top, air inlet pipe 21 is a blind pipe, inner core 2 places the closed chamber interior 11 of shell 1, constitute dehydration ring cavity 23 between the inwall of its cylindrical shell 22 peripheries and shell 1, and make the entrance point 211 of its top air inlet pipe 21 pass shell 1 communicating with the external world; The external diameter of dedusting eddy flow plate 3 is corresponding with cylindrical shell 22 internal diameters of inner core 2, and dedusting eddy flow plate 3 places in the cylindrical shell 22, and is positioned at the joining place of cylindrical shell 22 and air inlet pipe 21; As shown in Figure 2, moisture film structure 4 is slightly less than the annular enclosed cover of cylindrical shell 22 internal diameters of inner core 2 for external diameter, its outer wall is all established a plurality of spillway holes 41 and water inlet pipe 42, moisture film structure 4 places in inner core 2 cylindrical shells 22 and is positioned at the below of dedusting eddy flow plate 3, and water inlet pipe 42 passes the cylindrical shell 22 and the shell 1 of inner core 2 on it; Swash mist cover 5 and be bell mouth shape, swash mist cover 5 and place in the closed chamber 11 of shell 1 and be positioned at the below of inner core 2, and make the cylindrical shell 22 bottom outer rims of inner wall surface thereof 51 and inner core 2 constitute ring-types swashing mist gap 52 with arc inner wall face 51; Dehydrated structure 6 is made up of three groups of ring baffle plates 61,62,63, and ring baffle plate 61,62,63 is disposed on respectively on the inwall of cylindrical shell 22 outer walls of inner core 2 and shell 1, and makes ring baffle plate 61,63 towards having a down dip; The external diameter of demist eddy flow plate 7 is corresponding with the internal diameter of the blast pipe 12 of shell 1, and places in the blast pipe 12, and its blind plate 71 is the major diameter blind plate, and its swirl vane 72 is the high inclination-angle swirl vane.
Surface at all parts that contact with flue gas of the present utility model all applies KP
1Heat-resisting acid-resistant anti-corrosion clay.
Claims (5)
1, a kind of compound Gas-Rotation-Plate Dust Separator, it is characterized in that it by shell, inner core, dedusting eddy flow plate, moisture film structure, swash mist cover, dehydrated structure and demist eddy flow plate and form, shell is for constituting the hollow housing of closed chamber, and its top is provided with the blast pipe that connects with closed chamber; Inner core is the shell-like cylindrical shell that the top is provided with air inlet pipe, and inner core places in the closed chamber of shell, constitutes the dehydration ring cavity between the inwall of its cylindrical shell periphery and shell, and makes its top air inlet pipe pass shell communicating with the external world; The external diameter of dedusting eddy flow plate is corresponding with the inner core cylinder internal diameter, and it places in the cylindrical shell, and is positioned at the joining place of cylindrical shell and air inlet pipe; The moisture film structure has the annular enclosed cover that external diameter is slightly less than the inner core cylinder internal diameter, and its outer wall is all established a plurality of spillway holes and water inlet pipe, and the moisture film structure places in the inner core cylindrical shell and is positioned at the below of dedusting eddy flow plate, and water inlet pipe passes inner core cylindrical shell and shell on it; Swash the mist cover and be bell mouth shape, sharp mist is placed in the closed chamber of shell and is positioned at the inner core below, and makes inner wall surface thereof and inner core cylindrical shell bottom outer rim constitute the sharp mist gap of ring-type; Dehydrated structure is made up of ring baffle plate more than two groups, and annular flap is disposed on inner core cylinder body outer wall and the outer casing inner wall; The external diameter of demist eddy flow plate is corresponding with the blast pipe internal diameter of shell, and places in the blast pipe.
2, compound Gas-Rotation-Plate Dust Separator according to claim 1 is characterized in that the bottom of described shell constitutes water storage cavity and the grey chamber that is truncation reverse taper shape successively, is provided with valve between water storage cavity and the grey chamber, and bottom, grey chamber is provided with ash hole; The shell periphery is provided with overflow structure and ash position detection architecture, and the overflow structure is positioned at predetermined level height place; Ash position detection architecture is made up of ash position plate, conduit, flexible element, guide wheel and weight, ash position plate places grey chamber inside top, one end of conduit is connected with top, grey chamber, and connect with grey chamber, guide wheel is installed in the other end of conduit, one end of flexible element is connected with ash position plate, and its other end is connected with weight after passing conduit, pile warp guide wheel.
3, compound Gas-Rotation-Plate Dust Separator according to claim 1 and 2, the port of export that it is characterized in that described blast pipe are provided with secondary ash chamber, and secondary ash chamber upper and lower be respectively equipped with take out in the machine gas outlet and the ash hole that are connected.
4, compound Gas-Rotation-Plate Dust Separator according to claim 1 and 2 is characterized in that described sharp mist cover has the arc inner wall face.
5, compound Gas-Rotation-Plate Dust Separator according to claim 1 and 2, the blind plate that it is characterized in that described demist eddy flow plate is the major diameter blind plate, its swirl vane is the high inclination-angle swirl vane.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 96244696 CN2278521Y (en) | 1996-12-10 | 1996-12-10 | Double swirl blade dust-remover |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 96244696 CN2278521Y (en) | 1996-12-10 | 1996-12-10 | Double swirl blade dust-remover |
Publications (1)
Publication Number | Publication Date |
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CN2278521Y true CN2278521Y (en) | 1998-04-15 |
Family
ID=33917997
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 96244696 Expired - Fee Related CN2278521Y (en) | 1996-12-10 | 1996-12-10 | Double swirl blade dust-remover |
Country Status (1)
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CN (1) | CN2278521Y (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104355142A (en) * | 2014-11-07 | 2015-02-18 | 南通密炼捏合机械有限公司 | Conveying device used after cotton or wood pulp paper velvet forming in CMC (carboxy methyl cellulose) production |
CN105999975A (en) * | 2016-08-01 | 2016-10-12 | 中冶京诚工程技术有限公司 | Dust removal defogging device |
CN106422705A (en) * | 2016-11-07 | 2017-02-22 | 大连科林能源工程技术开发有限公司 | Multi-stage fluidized washing and resourceful utilization ultra-low pollutant discharge system for sulfur-containing waste gas |
CN111991966A (en) * | 2020-08-21 | 2020-11-27 | 上海应用技术大学 | Multistage cyclone wet dust collector |
CN114425207A (en) * | 2020-09-17 | 2022-05-03 | 中国石油化工股份有限公司 | Gas dust removal device and dust removal filler thereof |
-
1996
- 1996-12-10 CN CN 96244696 patent/CN2278521Y/en not_active Expired - Fee Related
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104355142A (en) * | 2014-11-07 | 2015-02-18 | 南通密炼捏合机械有限公司 | Conveying device used after cotton or wood pulp paper velvet forming in CMC (carboxy methyl cellulose) production |
CN105999975A (en) * | 2016-08-01 | 2016-10-12 | 中冶京诚工程技术有限公司 | Dust removal defogging device |
CN106422705A (en) * | 2016-11-07 | 2017-02-22 | 大连科林能源工程技术开发有限公司 | Multi-stage fluidized washing and resourceful utilization ultra-low pollutant discharge system for sulfur-containing waste gas |
CN111991966A (en) * | 2020-08-21 | 2020-11-27 | 上海应用技术大学 | Multistage cyclone wet dust collector |
CN114425207A (en) * | 2020-09-17 | 2022-05-03 | 中国石油化工股份有限公司 | Gas dust removal device and dust removal filler thereof |
CN114425207B (en) * | 2020-09-17 | 2023-01-10 | 中国石油化工股份有限公司 | Gas dust removal device and dust removal filler thereof |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
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 |