CN204224624U - The thick collection device of a kind of blast furnace gas dust - Google Patents
The thick collection device of a kind of blast furnace gas dust Download PDFInfo
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- CN204224624U CN204224624U CN201420713309.0U CN201420713309U CN204224624U CN 204224624 U CN204224624 U CN 204224624U CN 201420713309 U CN201420713309 U CN 201420713309U CN 204224624 U CN204224624 U CN 204224624U
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- gas
- blast furnace
- gas pipe
- dust
- eddy flow
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Abstract
The utility model discloses the thick collection device of a kind of blast furnace gas dust, comprise housing, gas pipe, reverse taper and dividing plate; Described housing upper is provided with gas exit, described gas pipe top is provided with gas entry, bottom is provided with expansion segment, described gas pipe is vertically arranged in the housing, described dividing plate is suspended between gas pipe expansion segment and inner walls, and region separation between gas pipe expansion segment and inner walls is become gas channel and wall circuit, described reverse taper to be fixedly installed on gas pipe outer wall and corresponding shutoff above dividing plate, be connected by eddy flow section between described gas channel with wall circuit; This device effectively combines the advantage of gravity and cyclone dust removal equipment, achieve two-stage in same device and receive powder, improve the efficiency that powder is received in thick dedusting, alleviate the load of follow-up bag-type dust, reduce the wear rate of dust to equipment, extend the work-ing life of receipts powder device and decrease maintenance of the equipment amount.
Description
Technical field
The utility model belongs to blast furnace gas purification technical field, is specifically related to the thick collection device of a kind of blast furnace gas dust.
Background technology
One of the byproduct that blast-furnace smelting produces blast furnace gas, the main fuel of Chang Zuowei hotblast stove, coke oven, process furnace, power plant boiler etc., it is the important energy source that Steel Plant run, its degree of purification directly affects the use of combustion equipment in downstream process, when dust content is higher, can cause the blocking of pipeline and combustion equipment, the scorification of refractory materials and equipment corrosion wearing and tearing etc., the raising required along with smelting technology and environment protection emission, also has higher requirement to gas purification.
The blast furnace gas that current blast furnace ironmaking produces, its purification is all add smart dedusting two-stage by thick dedusting to complete, and thick dedusting many employings gravitational precipitator, also has the cyclone dust removal adopting external PW, smart dedusting many employings wet scrubbing dedusting and dry-method bag-type dust collecting.Gravitational precipitator have structure simple, invest low, working cost is low, the advantages such as little are damaged in easy care and resistance, but its efficiency is lower.Cyclone duster structure is more complicated, equipment attrition is serious, resistance is damaged comparatively large, but efficiency of dust collection is high.Wet scrubbing dedusting floor space is large, system complex, easily blocking, maintenance workload are large, and dry-method bag-type dust collecting take up an area little, system is simple, gas temperature is high, efficiency advantages of higher.Therefore the smart dedusting that the current thick dedusting with gravitational dust collection adds dry method dust is combined into the main flow of blast furnace gas purification development.
Gravity adds the combination of bag-type dust from current operation, still need perfect aspect, the thick efficiency of dust collection of gravity is low, especially along with the increase of combustion intensity, in order to control smelting cost crude fuel condition again in reduction situation, coal gas amount and coal gas are containing Dust Capacity also along with increase, and load of dust remove also increases accordingly, and such cloth bag is in heavy-duty service situation, occur that cloth bag is fragile, the phenomenon that efficiency of dust collection reduces.
Summary of the invention
In view of this, the purpose of this utility model is to provide a kind of blast furnace gas dust thick collection device, is intended to the advantage organically in conjunction with gravity and cyclone dust removal, improves the efficiency of thick dedusting, alleviate the load of follow-up bag-type dust; In addition while the thick efficiency of dust collection of raising, reduce the wearing and tearing of equipment, extend its work-ing life.
For achieving the above object, the utility model provides following technical scheme: the thick collection device of a kind of blast furnace gas dust, is characterized in that: comprise housing, gas pipe, reverse taper and dividing plate; Described housing upper is provided with gas exit, described gas pipe top is provided with gas entry, bottom is provided with expansion segment, described gas pipe is vertically arranged in the housing, described dividing plate is suspended between gas pipe expansion segment and inner walls, and region separation between gas pipe expansion segment and inner walls is become gas channel and wall circuit, described reverse taper to be fixedly installed on gas pipe outer wall and corresponding shutoff above dividing plate, be connected by eddy flow section between described gas channel with wall circuit.
Further, described eddy flow section for being arranged on the spinning disk between dividing plate and reverse taper, the angle of rotation β of described spinning disk
1≤ 90 °.
Further, the angle of rotation β of described spinning disk
1it is 20 ° ~ 70 °.
Further, described eddy flow section is that several are arranged on the eddy flow passage between dividing plate and reverse taper, the angle of rotation β of described eddy flow passage
2≤ 90 °.
Further, the angle of rotation β of described eddy flow passage
2it is 20 ° ~ 70 °.
Further, described eddy flow section is for being opened in the eddy flow through hole on dividing plate.
Further, expansion angle α≤45 ° of described gas pipe expansion segment.
Further, also comprise dust retaining cone body, described dust retaining cone body correspondence is suspended between gas pipe expansion segment and housing bottom.
The beneficial effects of the utility model are: this apparatus structure is simple, cheap, use and maintenance convenient, effectively combine the advantage of gravity and cyclone dust removal equipment, achieve two-stage in same device and receive powder, improve the efficiency that powder is received in thick dedusting, alleviate the load of follow-up bag-type dust; First gravity collects big dust particle, then eddy flow collects small-particle dust, reduces the wear rate of dust to equipment, overcomes the shortcoming of existing cyclone dust removal, extends the work-ing life of receipts powder device and decreases maintenance of the equipment amount.
Accompanying drawing explanation
In order to make the purpose of this utility model, technical scheme and beneficial effect clearly, the utility model provides following accompanying drawing to be described:
Fig. 1 is the collection device structural representation of band spinning disk;
Fig. 2 is the collection device structural representation of band eddy flow passage;
Fig. 3 is the collection device structural representation of band eddy flow through hole;
Fig. 4 is the collection device structural representation of band dust retaining cone body;
Fig. 5 is that the A-A of Fig. 1 is to sectional view;
Fig. 6 is that the B-B of Fig. 2 is to sectional view.
Embodiment
Below in conjunction with accompanying drawing, preferred embodiment of the present utility model is described in detail.
As shown in the figure, the thick collection device of blast furnace gas dust in the present invention, is characterized in that: comprise housing 10, gas pipe, reverse taper 5 and dividing plate 4; Described housing 10 top is provided with gas exit 9, described gas pipe top is provided with gas entry 1, bottom is provided with expansion segment 2, described gas pipe is vertically arranged in the housing 10, described dividing plate 4 is suspended between gas pipe expansion segment 2 and housing 10 inwall, and region separation between gas pipe expansion segment 2 and housing 10 inwall is become gas channel 6 and wall circuit 8, described reverse taper 5 to be fixedly installed on gas pipe outer wall and corresponding shutoff above dividing plate 4, described gas channel 6 is connected by eddy flow section with between wall circuit 8.
In the present embodiment, the bevel arm piece that gas entry 1 is steel-pipe welding, the up-small and down-big taper(ed)pipe that expansion segment 2 is Plate Welding, gas pipe is vertically arranged on the center of housing 10, the downtake of blast furnace is connected with gas entry 1, from top to bottom vertical expansion segment 2 is entered in the axial direction from gas entry 1 from blast furnace roof band dust blast furnace gas out, air-flow reduces gradually at expansion segment flow velocity, do not produce swirling two-phase flows, rely on gravity big dust particle to be collected in bottom housing 10 3.Dividing plate 4 is the ring flat-plate of fixing welding on the housing 10, reverse taper 5 changes from small to big for diameter, reducing cone from large to small again, the reverse taper 5 of steel is fixed on the expansion segment 2 outer wall place above dividing plate 4, housing 10, expansion segment 2, dividing plate 4 and reverse taper 5 form gas channel 6 jointly, eddy flow section and wall circuit 8, gas channel 6 forces the both sides from bottom to top countercurrent flow of blast furnace gas along expansion segment 2 with remaining dust, air-flow produces rotational flow through eddy flow section, collide with wall under the influence of centrifugal force, relatively fine particle to be then deposited to bottom housing 10 3 along wall circuit 8, blast furnace gas finally with fine powder enters next step operation by top gas exit 9 discharge.
Eddy flow section has various structures form, the eddy flow section in the present embodiment for being arranged on the spinning disk 11 between dividing plate 4 and reverse taper 5, as shown in Figure 1.Spinning disk 11 upper end is welded with reverse taper 5, and lower end is welded with dividing plate 4.Spinning disk 11 can select the movable spinning disk of fixed spinning disk or adjustable angle, spinning disk 11 angle of rotation β in the horizontal plane
1≤ 90 °; Wherein, angle of rotation β
1the value wear pattern that can damage situation and spinning disk 11 according to the resistance of the collection effciency of dust, flow of gas comprehensively determine; Preferably, spinning disk 11 angle of rotation β in the horizontal plane
1it is 20 ° ~ 70 °.In order to extend the work-ing life of spinning disk 11 further, spinning disk 11 can also arrange abrasion-proof backing block above.
As the alternative of such scheme, described eddy flow section also can be several and is arranged on eddy flow passage 12 between dividing plate 4 and reverse taper 5, and air-flow, after eddy flow passage flows out, also form rotational flow, as shown in Figure 2.Described eddy flow passage 12 in the horizontal plane angle of rotation β
2≤ 90 °; Wherein, angle of rotation β
2the value wear pattern that can damage situation and eddy flow passage 12 according to the resistance of the collection effciency of dust, flow of gas comprehensively determine; Preferably, eddy flow passage 12 angle of rotation β in the horizontal plane
2it is 20 ° ~ 70 °.Certainly, also abrasion-proof backing block can be set on eddy flow passage 12, extend the work-ing life of eddy flow passage 12 further.
As the alternative of such scheme, described eddy flow section for being opened in the eddy flow through hole 14 on dividing plate 4, as shown in Figure 3.Namely the direct shutoff of reverse taper 5 is above gas channel 6, air-flow only relies on the shape of reverse taper 5 to change the flow direction, in gas channel 6, air-flow is from bottom to top flowed out by eddy flow through hole 14, inertial impaction is there is with reverse taper 5 and housing 10, part particle is rebounded or is deposited in wall circuit 8, and powder is received at the two poles of the earth that also can realize blast furnace gas.Certainly, in this kind of structure, the chance of air-flow and collision with wall is less than the structure adding spinning disk 11 and eddy flow passage 12, so its collection effciency is a little less than structure in front two.
In the present embodiment, expansion angle α≤45 ° of described gas pipe expansion segment 2, in this angular range, blast furnace gas can not produce swirling two-phase flows in gas pipe, and the one-level that can complete blast furnace gas to greatest extent receives powder.
In the present embodiment, also comprise dust retaining cone body 13, described dust retaining cone body 13 correspondence is suspended in bottom gas pipe expansion segment 2 and housing 10 between 3, can effectively prevent reentrainment of dust phenomenon.Concrete, with dust air-flow from expansion segment 2 out after flowing-path change into from the bottom to top, can be formed like this to turn and inhale, cause reentrainment of dust phenomenon (dust being about to sedimentation is taken away again), bottom housing 10,3 arrange dust retaining cone body 13, namely the dust of sedimentation falls within below cone, thus avoids air-flow and transfer dust, improves dust collection efficiency.
The thick collection method of blast furnace gas dust of this device, mainly comprises the following steps:
(1) blast furnace gas from top to bottom enters from gas entry, first passes through vertical expansion segment 2, does not produce swirling two-phase flows, and macrobead coal gas dust collection is bottom housing 10 3 under gravity, and the one-level completing blast furnace gas receives powder;
(2) blast furnace gas through sedimentation rises along gas channel 6 with residue dust;
(3) blast furnace gas that rises of band residue dust is through eddy flow section, and under the effect of centrifugal force and mutual impact force, comparatively fine dusts to be deposited to bottom housing 10 3 along wall circuit 8, and the secondary completing blast furnace gas receives powder;
(4) be with the blast furnace gas of fine dusts to be discharged by the gas exit 9 on housing 10 top, namely complete the thick collection of blast furnace gas dust, the blast furnace gas of discharging from gas exit 9 then enters next step operation continuation process.All processes of this thick collection method all complete in same housing, and process is simple, and collection effciency is high.
What finally illustrate is, above preferred embodiment is only in order to illustrate the technical solution of the utility model and unrestricted, although be described in detail the utility model by above preferred embodiment, but those skilled in the art are to be understood that, various change can be made to it in the form and details, and not depart from the utility model claims limited range.
Claims (8)
1. the thick collection device of blast furnace gas dust, is characterized in that: comprise housing, gas pipe, reverse taper and dividing plate; Described housing upper is provided with gas exit, described gas pipe top is provided with gas entry, bottom is provided with expansion segment, described gas pipe is vertically arranged in the housing, described dividing plate is suspended between gas pipe expansion segment and inner walls, and region separation between gas pipe expansion segment and inner walls is become gas channel and wall circuit, described reverse taper to be fixedly installed on gas pipe outer wall and corresponding shutoff above dividing plate, be connected by eddy flow section between described gas channel with wall circuit.
2. the thick collection device of blast furnace gas dust according to claim 1, is characterized in that: described eddy flow section for being arranged on the spinning disk between dividing plate and reverse taper, the angle of rotation β of described spinning disk
1≤ 90 °.
3. the thick collection device of blast furnace gas dust according to claim 2, is characterized in that: the angle of rotation β of described spinning disk
1it is 20 ° ~ 70 °.
4. the thick collection device of blast furnace gas dust according to claim 1, is characterized in that: described eddy flow section is that several are arranged on the eddy flow passage between dividing plate and reverse taper, the angle of rotation β of described eddy flow passage
2≤ 90 °.
5. the thick collection device of blast furnace gas dust according to claim 4, is characterized in that: the angle of rotation β of described eddy flow passage
2it is 20 ° ~ 70 °.
6. the thick collection device of blast furnace gas dust according to claim 1, is characterized in that: described eddy flow section is for being opened in the eddy flow through hole on dividing plate.
7. the thick collection device of blast furnace gas dust according to claim 1, is characterized in that: expansion angle α≤45 ° of described gas pipe expansion segment.
8. the thick collection device of blast furnace gas dust according to any one of claim 1 to 7, is characterized in that: also comprise dust retaining cone body, and described dust retaining cone body correspondence is suspended between gas pipe expansion segment and housing bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420713309.0U CN204224624U (en) | 2014-11-24 | 2014-11-24 | The thick collection device of a kind of blast furnace gas dust |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420713309.0U CN204224624U (en) | 2014-11-24 | 2014-11-24 | The thick collection device of a kind of blast furnace gas dust |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204224624U true CN204224624U (en) | 2015-03-25 |
Family
ID=52922742
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420713309.0U Withdrawn - After Issue CN204224624U (en) | 2014-11-24 | 2014-11-24 | The thick collection device of a kind of blast furnace gas dust |
Country Status (1)
| Country | Link |
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| CN (1) | CN204224624U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104328234A (en) * | 2014-11-24 | 2015-02-04 | 中冶赛迪工程技术股份有限公司 | Rough collection device and method for gas and dust from blast furnace |
| CN108714819A (en) * | 2018-06-29 | 2018-10-30 | 菲斯达排放控制装置（苏州）有限公司 | The preposition efficient slagging-off protective device of numerically-controlled machine tool coolant recirculation pump |
-
2014
- 2014-11-24 CN CN201420713309.0U patent/CN204224624U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104328234A (en) * | 2014-11-24 | 2015-02-04 | 中冶赛迪工程技术股份有限公司 | Rough collection device and method for gas and dust from blast furnace |
| CN108714819A (en) * | 2018-06-29 | 2018-10-30 | 菲斯达排放控制装置（苏州）有限公司 | The preposition efficient slagging-off protective device of numerically-controlled machine tool coolant recirculation pump |
| CN108714819B (en) * | 2018-06-29 | 2024-06-07 | 菲斯达排放控制装置（苏州）有限公司 | Prepositive deslagging protection device of cooling liquid circulating pump of numerical control machine tool |
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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 |
Granted publication date: 20150325 Effective date of abandoning: 20160316 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |