CN103757155A - Coke dry quenching water mist granulation device - Google Patents
Coke dry quenching water mist granulation device Download PDFInfo
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- CN103757155A CN103757155A CN201310732280.0A CN201310732280A CN103757155A CN 103757155 A CN103757155 A CN 103757155A CN 201310732280 A CN201310732280 A CN 201310732280A CN 103757155 A CN103757155 A CN 103757155A
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- water mist
- granulation
- slag
- spray nozzle
- spraying nozzle
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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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
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- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
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Abstract
The invention discloses a coke dry quenching water mist granulation device, belonging to the field of coke dry quenching granulation. The coke dry quenching water mist granulation device comprises a granulation device body, a slag path for furnace slag, a rotating cup, a granulation slag outlet, a gas outlet, a main shaft, a bearing as well as a water mist spray nozzle, wherein the water mist spray nozzle comprises a spray hole, a converging cavity, a rotary valve and a threaded interface, and the water mist spray nozzle is divided into 4-8 parts to be fixed on the periphery in the granulation device body; the gas outlet is communicated with a granulation bin above the granulation device body; the water mist spray nozzle is shaped like an animal horn; a mixing cavity is arranged in the water mist spray nozzle, the rotary valve is arranged in the mixing cavity of the spray nozzle, and the spray hole communicated with the mixing cavity is formed at the front end of the spray nozzle. The coke dry quenching water mist granulation device disclosed by the invention adopts water mist granulation and has the advantages of enabling the granulation degree of high-temperature liquid slag to be more obvious, utilizing the afterheat after purification of high-temperature flue gas, saving energy, simultaneously reducing atmospheric pollution and the like.
Description
Technical field
The invention belongs to granulating device field, particularly a kind of high temperature molten slag granulating device.
Background technology
In recent years, due to the utilizability of high temperature furnace slag, recyclable high temperature furnace slag waste heat not only, also can utilize the waste material of high temperature furnace slag.In the prior art, Iron And Steel Industry waste residue a kind of to recycle method be using further fine grinding and as the raw material of Cement industry after slag granulation.It is also the domestic main method of utilizing blast-furnace slag.It not only plays an important role to environment protection, can also produce very significant technical economic benefit.
Domestic main blast-furnace slag granulated processed method is grain slag facture at present, that is stokehold water quenching.Their main technological features is that in flowing to high-temperature slag when tap cinder, inject high pressure water makes slag chilling, thereby obtains grain slag.There is following problem in Water Quenching method: consumes a large amount of new water resourcess; The waste heat of slag cannot reclaim; Element in slag enters water vapour and produces S0
2and H
2s etc. bring atmospheric pollution.Therefore can adopt dry method cooling, when dry method is cooling, need granulation, be convenient to the abundant recovery of its cooling and waste heat in fluidized-bed.Conventionally the melt cinder pelletizer adopting has a kind of wind granulation; be that air blast operation machine is set under slag storehouse; the high-speed air flow that melt cinder blows out with gas blower when slag storehouse end flows out contacts; and rapid granulation, being blown to afterwards on water wall, melt cinder condenses into solid-state in operational process from liquid state; this wind granulation can be utilized the sensible heat of slag; but the cooling performance of high temperature melt cinder is bad, also have a lot of sensible heats fully not absorb, and traditional wind granulation degree is not high.
Summary of the invention
The technical problem solving:
Tradition water quenching can not make full use of the sensible heat of molten slag, and the broken degree of traditional wind is not high, and cooling performance is bad, and sensible heat absorbs insufficient.
Technical scheme:
For addressing the above problem; a kind of dry pulp water droplet gasifying device that puts out; comprise granulating device body, slag slag road, rotating cup, grain slag outlet, pneumatic outlet, main shaft and bearing; also comprise spraying nozzle; described spraying nozzle comprises spray orifice, converges chamber, stopcock and hickey, and spraying nozzle divides 4--8 to be fixed on granulating device body interior surrounding.
Described pneumatic outlet communicates with granulation storehouse above granulating device body.
Described spraying nozzle is beast horn shape.
In described spraying nozzle, have hybrid chamber, in the hybrid chamber of nozzle, stopcock is housed, the front end of nozzle has the spray orifice being communicated with hybrid chamber.
Beneficial effect of the present invention:
1, the present invention adopts water smoke granulation, makes the granulation degree of high temperature melt cinder more obvious;
2, after high-temperature flue gas purification, can carry out UTILIZATION OF VESIDUAL HEAT IN, save energy has reduced topsoil simultaneously.
Accompanying drawing explanation
Fig. 1 is the structural representation of apparatus of the present invention;
Fig. 2 is the structural representation of spraying nozzle 3;
In figure:
1, grain slag outlet 2, granulation storehouse 3, spraying nozzle 4, granulating device body 5, pneumatic outlet 6, slag slag road 7, rotating cup 8, main shaft and bearing 9, spray orifice 10, converge chamber 11, stopcock 12, hickey.
Embodiment
For technique means, character of innovation that the present invention is realized, reach object and effect is easy to understand, below in conjunction with concrete diagram, further set forth the present invention.
The invention provides the existing duster system of a kind of solution complicated, floor space is large, the expensive a kind of dry pulp water droplet gasifying device that puts out with high investment.
A kind of dry pulp water droplet gasifying device that puts out as shown in Figure 1, comprise granulating device body 4, slag slag road 6, rotating cup 7, grain slag outlet 1, pneumatic outlet 5, main shaft and bearing 8, it is characterized in that: also comprise spraying nozzle 3, described spraying nozzle 3 comprises spray orifice 9, converges chamber 10, stopcock 11 and hickey 12, and 4--8, spraying nozzle 3 minutes is fixed on the inner surrounding of granulating device body 4; Pneumatic outlet 5 communicates with granulation storehouse 2 above granulating device body 4; Spraying nozzle 3 is beast horn shape; In spraying nozzle 3, have the chamber of converging 10, stopcock 11 is equipped with in converging of spraying nozzle 3 in chamber 10, and the front end of spraying nozzle 3 has and the spray orifice 9 that converges chamber 10 and be communicated with.
Based on above-mentioned principle, a kind of dry pulp water droplet gasifying device that puts out as described in Figure 1, in use, blast furnace melt cinder is broken up into small grain size melt cinder while flowing to the rotating cup 7 of high speed rotating by slag slag road 6; Meanwhile, from water blast gun, flow into the high pressure water of spraying nozzle 3 through stopcock 11, converge converging chamber 10, and pass through in spray orifice 9 spirt granulation storehouses and form water smoke, in granulation storehouse 2, water smoke and dispersed small grain size melt cinder form convection current, and carry out heat exchange, water smoke is vaporization rapidly at high temperature, the little melt cinder sensible heat of high temperature is absorbed, and temperature declines rapidly, and the high-temperature smoke of generation rises, by pneumatic outlet 5, discharge purify, dedusting, and it is carried out to waste heat recovery; The little slag particle of solid in the 2 interior formation of granulation storehouse is discharged from grain slag outlet 1.
Claims (4)
1. the dry pulp water droplet gasifying device that puts out; comprise granulating device body (4), slag slag road (6), rotating cup (7), grain slag outlet (1), pneumatic outlet (5), main shaft and bearing (8); it is characterized in that: also comprise spraying nozzle (3); described spraying nozzle (3) comprises spray orifice (9), converges chamber (10), stopcock (11) and hickey (12), and spraying nozzle (3) is fixed on the inner surrounding of granulating device body (4).
2. a kind of high-temperature water droplet gasifying device as claimed in claim 1, is characterized in that: described spraying nozzle (3) is ox horn shape, has 4-8.
3. a kind of dry pulp water droplet gasifying device that puts out as claimed in claim 1, is characterized in that: described pneumatic outlet (5) communicates with granulation storehouse (2) in granulating device body (4) top.
4. a kind of dry pulp water droplet gasifying device that puts out as claimed in claim 1; it is characterized in that: in described spraying nozzle (3), have the chamber of converging (10); stopcock (11) is equipped with in converging of spraying nozzle (3) in chamber (10), the front end of spraying nozzle (3) has and the spray orifice (9) that converges chamber (10) and be communicated with.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201310732280.0A CN103757155A (en) | 2013-12-27 | 2013-12-27 | Coke dry quenching water mist granulation device |
Applications Claiming Priority (1)
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CN201310732280.0A CN103757155A (en) | 2013-12-27 | 2013-12-27 | Coke dry quenching water mist granulation device |
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CN103757155A true CN103757155A (en) | 2014-04-30 |
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CN201310732280.0A Pending CN103757155A (en) | 2013-12-27 | 2013-12-27 | Coke dry quenching water mist granulation device |
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105624347A (en) * | 2016-03-11 | 2016-06-01 | 西安交通大学 | Liquid high-temperature slag granulation and waste heat recovery device |
CN105624348A (en) * | 2016-03-11 | 2016-06-01 | 西安交通大学 | System for granulating high-temperature molten slag |
CN108796148A (en) * | 2018-09-05 | 2018-11-13 | 安徽工业大学 | A kind of granulated method of blast furnace slag rotation |
CN108796147A (en) * | 2018-09-05 | 2018-11-13 | 安徽工业大学 | A kind of blast furnace slag granulation and the method for waste heat recovery |
CN108796149A (en) * | 2018-09-05 | 2018-11-13 | 安徽工业大学 | A kind of equipment for granulation of slag of grading |
CN108796150A (en) * | 2018-09-05 | 2018-11-13 | 安徽工业大学 | A kind of granulated device of blast furnace slag rotation |
CN108998604A (en) * | 2018-09-05 | 2018-12-14 | 安徽工业大学 | A kind of blast furnace slag granulation and the device of waste heat recycling |
CN109022646A (en) * | 2018-09-05 | 2018-12-18 | 安徽工业大学 | A kind of slag granulation method of grading |
-
2013
- 2013-12-27 CN CN201310732280.0A patent/CN103757155A/en active Pending
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105624347A (en) * | 2016-03-11 | 2016-06-01 | 西安交通大学 | Liquid high-temperature slag granulation and waste heat recovery device |
CN105624348A (en) * | 2016-03-11 | 2016-06-01 | 西安交通大学 | System for granulating high-temperature molten slag |
CN105624348B (en) * | 2016-03-11 | 2018-03-02 | 西安交通大学 | One kind is used for high-temperature liquid state slag granulating system |
CN105624347B (en) * | 2016-03-11 | 2018-12-07 | 西安交通大学 | A kind of liquid high-temperature slag granulation and waste-heat recovery device |
CN108796148A (en) * | 2018-09-05 | 2018-11-13 | 安徽工业大学 | A kind of granulated method of blast furnace slag rotation |
CN108796147A (en) * | 2018-09-05 | 2018-11-13 | 安徽工业大学 | A kind of blast furnace slag granulation and the method for waste heat recovery |
CN108796149A (en) * | 2018-09-05 | 2018-11-13 | 安徽工业大学 | A kind of equipment for granulation of slag of grading |
CN108796150A (en) * | 2018-09-05 | 2018-11-13 | 安徽工业大学 | A kind of granulated device of blast furnace slag rotation |
CN108998604A (en) * | 2018-09-05 | 2018-12-14 | 安徽工业大学 | A kind of blast furnace slag granulation and the device of waste heat recycling |
CN109022646A (en) * | 2018-09-05 | 2018-12-18 | 安徽工业大学 | A kind of slag granulation method of grading |
CN108796150B (en) * | 2018-09-05 | 2020-08-04 | 安徽工业大学 | Rotary granulating device for blast furnace slag |
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Application publication date: 20140430 |