CN202519281U - Blast furnace gas purification device - Google Patents
Blast furnace gas purification device Download PDFInfo
- Publication number
- CN202519281U CN202519281U CN 201220074257 CN201220074257U CN202519281U CN 202519281 U CN202519281 U CN 202519281U CN 201220074257 CN201220074257 CN 201220074257 CN 201220074257 U CN201220074257 U CN 201220074257U CN 202519281 U CN202519281 U CN 202519281U
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- blast furnace
- furnace gas
- gas purification
- purification device
- water
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Abstract
The utility model relates to recovery devices of blast furnace gas, in particular to a blast furnace gas washing purification treatment device. The blast furnace gas purification device is composed of a first grade venturi dust remover, a second grade venturi dust remover, a rotational flow settling pond, a hot water pond, a water circulating pump, a filter and a wash water sprinkling device. The blast furnace gas purification device is characterized in that the first grade venturi dust remover and the second grade venturi dust remover which are connected are both connected with a pipeline of the rotational flow settling pond, the wash water sprinkling device is composed of an upper atomization watering device and a lower atomization watering device which are respectively arranged above venturi tube throats of the first grade venturi dust remover and the second grade venturi dust remover and inside the venturi tube throats, and the upper atomization watering device and the lower atomization watering device are connected with the hot water pond through a pipeline, a valve, the filter and the water circulating pump. The blast furnace gas purification device has the advantages of being novel in conception, simplified in structure, reasonable in configuration, smooth in dedusting and purifying process of gas and good in purification effect. Besides, by means of the blast furnace gas purification device, the problems like damages of the throats and blocking of the watering devices are solved, service life of equipment is prolonged, water consumption of wash water is reduced greatly, electricity consumption is saved, a cooling tower and an upper column pump package are saved, investment is reduced, maintenance and operation cost is saved greatly, outlet temperature of purified gas is increased, pressure loss of the blast furnace gas in the process of passing the throats is reduced, and blast furnace top gas recovery turbine unit (TRT) electric energy production is increased.
Description
Technical field
The utility model belongs to the blast furnace gas retrieving arrangement, relates in particular to blast furnace gas washing, purifying treatment unit.
Background technology
Blast furnace produces a large amount of blast furnace gases in smelting process, its dustiness still reaches 10～12g/m after the gravitational precipitator dedusting
3, further could use after the udst separation.Current blast furnace gas adopts two civilian formula cleaning apparatus washing, purifyings.This device is by one-level venturi tube and aditus laryngis grain of rice valve, gravity dehydration device, secondary venturi tube and grain of rice valve, filler water trap, sprinkler system, water circulating pump, hot tub, cooling tower, goes up compositions such as tower pump group, cyclone sediment pond.After effusive half purified gas of gravitational precipitator gets into the washing of one-level literary composition formula fly-ash separator, dehydration, get into the washing of secondary literary composition formula fly-ash separator, dehydration again.Blast furnace gas after the purification is through TRT top pressure power generation, and a part of heat supply wind furnace burns stove usefulness, and another part gets into gaspipe network; Its washing water operational scheme is: " partly purifying waste water " that the cyclone sediment pond overflows squeezed into cooling tower cooling back by the lift pump group and flowed into hot tub; Pump into civilian formula fly-ash separator sprinkler system by water circulating pump again; Blast furnace gas is carried out washing, purifying; Sewage after the washing flows back to the cyclone sediment pond through water discharge valve, so circulation.The shortcoming that exists of prior art is: (1) system energy consumption is high, water loss is big, and water loss is generally at 3.2～3.6L/m
3Between (WGR); (2) TRT inlet gas temperature low (general 50～55 ℃), the inlet outlet pressure differential of two civilian formula fly-ash separators influences its generated energy at 20～25kpa; (3) civilian formula aditus laryngis grain of rice valve is fragile; Its both sides water tank spiracle and top sprinkler system thereof are prone to stop up; Cause efficiency of dust collection to descend rapidly, make upstream device TRT top pressure power generation unit stator blade dust stratification, cause unit vibration, structure deteriorate; The carbonization of stove fillings superficial dust influences wind-warm syndrome and checker brick life-span.
The utility model content
In order to overcome the defective that prior art exists, the utility model discloses a kind of blast furnace gas purification device, blast furnace gas is carried out washing, purifying handle; Can solve aditus laryngis damages and the sprinkler system blockage problem; Reduce confluent, improve the gas purification effect, simplify circulation cleaning water conservancy project process flow; Cut down the consumption of energy, improve the TRT generated energy.
The blast furnace gas purification device is made up of one-level literary composition formula fly-ash separator, secondary literary composition formula fly-ash separator, cyclone sediment pond, hot tub, water circulating pump, strainer and washing water flusher.One-level, secondary literary composition formula fly-ash separator are connected; And all be communicated with cyclone sediment pond pipe connection; Hot tub is communicated with cyclone sediment pond pipe connection; Be characterized in that described washing water flusher is made up of last atomizing sprinkler system and following atomizing sprinkler system, be located at the top and the aditus laryngis inside of the cylindrical aditus laryngis of venturi tube of one-level, secondary literary composition formula fly-ash separator respectively; Upper and lower atomizing sprinkler system is connected by pipeline, valve, strainer, water circulating pump and hot tub.Effusive half purified gas of gravitational precipitator gets into one-level literary composition formula fly-ash separator, secondary literary composition formula fly-ash separator, washing, dehydration, and the blast furnace gas after the purification is through TRT top pressure power generation, and a part of heat supply wind furnace burns stove usefulness, and another part gets into gaspipe network; Washing water recycle process: " partly purifying waste water " that the cyclone sediment pond overflows flows into hot tub; Pump by water circulating pump;, strainer supplies atomizing sprinkler system and following atomizing water spraying device on the civilian formula fly-ash separator after filtering; Blast furnace gas is carried out washing, purifying, and the sewage after the washing flows back to the cyclone sediment pond through a literary composition, two civilian water discharge valves, recycles.
The utility model further improves, and the venturi tube aditus laryngis of described civilian formula fly-ash separator is designed to cylindrical.Air communication is even excessively, is difficult for laying dust, obstruction.
The utility model further improves, and the described atomizing sprinkler system of going up adopts 6-10 double helix atomizing lance, places venturi tube aditus laryngis top, with the washing water atomizing, increases the contact area of dust in washing water and the coal gas, not only anti-clogging plug but also water saving.
The utility model further improves, and described down atomizing sprinkler system adopts the bidirectional screw atomizing nozzle, and jet angle is 90 ° a cone, places aditus laryngis inner, and upwards, both direction sprays washing water downwards, water loss is little, does not stop up good dedusting effect.
Last improvement of the utility model, described strainer is a self-cleaning strainer, is located at water circulating pump exporter in the circulation cleaning water lines, good filtration effect helps preventing that waterworks from stopping up.
Compared with prior art, advantage is: novel, designs simplification, configuration are reasonable, and smooth and easy, the good purification of coal gas dust removal purification process solves better that aditus laryngis damages and the drawback of the obstruction of sprinkler system; Prolong service life of equipment, washing water purify water loss and reduce save electricity significantly; Cancellation cooling tower and last tower pump group reduce investment, save a large amount of maintenance and working cost; Improve and purify gas outlet temperature, the reduction blast furnace gas process aditus laryngis pressure-losses, raising TRT generated energy.
Description of drawings
The contrast accompanying drawing is described further the utility model below.
Fig. 1 is a blast furnace gas purification apparatus structure synoptic diagram.
Fig. 2 is the venturi tube structural representation of Fig. 1.
Embodiment
Embodiment 1 is with 2500m
3Blast furnace uses the blast furnace gas purification device to describe as example.
Can find out that by Fig. 1 the blast furnace gas purification device is made up of one-level literary composition formula fly-ash separator 1, secondary literary composition formula fly-ash separator 2, cyclone sediment pond 3, hot tub 4, water circulating pump 5, strainer 6 and washing water flusher.One-level literary composition formula fly-ash separator 1 is made up of venturi tube 7, gravity dehydration device 8; Venturi tube aditus laryngis 9 is cylindrical; Atomizing sprinkler system 10 is established in the aditus laryngis top; Following atomizing sprinkler system 11 is located in the aditus laryngis, and upper and lower atomizing sprinkler system is connected by pipeline, water supply valve door 12, strainer, water circulating pump and hot tub, supplies with washing water by water circulating pump.Establishing pipeline on the gravity dehydration device is connected with secondary literary composition formula dust remover roof; Divide into pipe drainage valve 13 and be connected, also establish pipeline, water discharging valve is connected with strainer with the cyclone sediment pond.Half purified gas is got into the atomizing washing water of last atomizing sprinkler system ejection by one-level literary composition formula dust remover roof and mixes; After getting into the venturi tube acceleration; Bump, absorb with the atomizing washing water drop that is located at the following atomizing sprinkler system ejection in the aditus laryngis again, behind the entering gravity dehydration device, dust and water droplet are separated from coal gas; Get into the cyclone sediment pond through valve; Overflow is to hot tub after deposition purifies, and the water circulating pump backup setting is delivered to upper and lower atomizing sprinkler system with the hot water pressurization through self-cleaning strainer, feedwater valve and carried out washing, purifying.Coal gas gets into secondary literary composition formula fly-ash separator again and purifies.Secondary literary composition formula fly-ash separator structure is identical with one-level literary composition formula fly-ash separator; What distinguish is that filler water trap 14 is set in the gravity dehydration device; The coal gas of separating from secondary literary composition formula fly-ash separator carries out second dehydration through the filler water trap, becomes purification coal gas, is seen off by pipeline; Through TRT generating, cooling, burning of heat supply wind furnace and entering gaspipe network.Adopt this gas cleaning device, the washing water loss reduces WGR 2.2-2.4L/m
3, save electricity improves the purification gas temperature more than 6 ℃, reduces the inlet outlet pressure differential 5kpa of two civilian formula fly-ash separators, and a ton iron generated energy improves 5kwh.
Can find out that by Fig. 2 the venturi tube aditus laryngis is cylindrical, simple and reasonable, makes central gas stream even, alleviate aditus laryngis wearing and tearing and knot dirt, prolong the aditus laryngis life-span.The atomizing sprinkler system is established on aditus laryngis top, is connected and composed by endless tube 15 and eight double helix atomizing lances, and the bidirectional screw atomizing nozzle is set in the aditus laryngis, upwards, spray washing water downwards, makes that dust-laden particle and washing water fully merge the raising dust removing effects in the coal gas.
Claims (5)
1. the blast furnace gas purification device is made up of one-level literary composition formula fly-ash separator (1), secondary literary composition formula fly-ash separator (2), cyclone sediment pond (3), hot tub (4), water circulating pump (5), strainer (6) and washing water flusher; Two-stage literary composition formula fly-ash separator is connected; And all be communicated with cyclone sediment pond pipe connection; Hot tub is communicated with cyclone sediment pond pipe connection; It is characterized in that described washing water flusher is made up of last atomizing sprinkler system (10) and following atomizing sprinkler system (11), be located at the top and the aditus laryngis inside of the cylindrical aditus laryngis of venturi tube (7) (9) of two-stage literary composition formula fly-ash separator respectively; Upper and lower atomizing sprinkler system is connected with hot tub by pipeline, valve, strainer, water circulating pump.
2. blast furnace gas purification device according to claim 1 is characterized in that the venturi tube aditus laryngis (9) of described civilian formula fly-ash separator is designed to cylindrical.
3. blast furnace gas purification device according to claim 1 is characterized in that the described atomizing sprinkler system (10) of going up adopts 6-10 double helix atomizing lance, places venturi tube aditus laryngis (9) top.
4. blast furnace gas purification device according to claim 1 is characterized in that described down atomizing sprinkler system (11) adopts the bidirectional screw atomizing nozzle, and jet angle is 90 ° a cone, places aditus laryngis inner, upwards, both direction sprays washing water downwards.
5. blast furnace gas purification device according to claim 1 is characterized in that described strainer (6) is a self-cleaning strainer, is located at the water circulating pump exporter of circulation cleaning water lines.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220074257 CN202519281U (en) | 2012-03-02 | 2012-03-02 | Blast furnace gas purification device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220074257 CN202519281U (en) | 2012-03-02 | 2012-03-02 | Blast furnace gas purification device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202519281U true CN202519281U (en) | 2012-11-07 |
Family
ID=47102241
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220074257 Withdrawn - After Issue CN202519281U (en) | 2012-03-02 | 2012-03-02 | Blast furnace gas purification device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202519281U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102586523A (en) * | 2012-03-02 | 2012-07-18 | 马钢(集团)控股有限公司 | Blast furnace gas purification plant |
| CN103894304A (en) * | 2014-04-15 | 2014-07-02 | 广东家美陶瓷有限公司 | Self-cleaning method and device for ceramic slurry spray-drying spraying gun |
| CN111502738A (en) * | 2020-04-30 | 2020-08-07 | 辽宁工程技术大学 | Dust control and removal device for mine driving working face and use method |
-
2012
- 2012-03-02 CN CN 201220074257 patent/CN202519281U/en not_active Withdrawn - After Issue
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102586523A (en) * | 2012-03-02 | 2012-07-18 | 马钢(集团)控股有限公司 | Blast furnace gas purification plant |
| CN102586523B (en) * | 2012-03-02 | 2013-08-07 | 马钢(集团)控股有限公司 | Blast furnace gas purification plant |
| CN103894304A (en) * | 2014-04-15 | 2014-07-02 | 广东家美陶瓷有限公司 | Self-cleaning method and device for ceramic slurry spray-drying spraying gun |
| CN111502738A (en) * | 2020-04-30 | 2020-08-07 | 辽宁工程技术大学 | Dust control and removal device for mine driving working face and use method |
| CN111502738B (en) * | 2020-04-30 | 2021-12-31 | 辽宁工程技术大学 | Dust control and removal device for mine driving working face and use method |
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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: 20121107 Effective date of abandoning: 20130807 |
|
| RGAV | Abandon patent right to avoid regrant |