CN201169596Y - Revolving furnace coal gas dry method cloth bag purification recovering device - Google Patents
Revolving furnace coal gas dry method cloth bag purification recovering device Download PDFInfo
- Publication number
- CN201169596Y CN201169596Y CNU2008200117890U CN200820011789U CN201169596Y CN 201169596 Y CN201169596 Y CN 201169596Y CN U2008200117890 U CNU2008200117890 U CN U2008200117890U CN 200820011789 U CN200820011789 U CN 200820011789U CN 201169596 Y CN201169596 Y CN 201169596Y
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- coal gas
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- gas
- pressure pulse
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Abstract
The utility model relates to a gas dry bag-type purification and recovery device for a converter, which is a device for recovering gas generated during the smelting process of the converter, wherein, an outlet of a heating boiler is connected with a telescopic joint; an outlet of the telescopic joint is connected with a water-sealed valve; an outlet of the water-sealed valve is connected with an inlet of an atomizing and cooling tank; an outlet of the atomizing and cooling tank is connected with an inlet of a duct fan; an outlet of the duct fan is connected with a tandem gas low-pressure pulse bag-type duster; a totally enclosed pneumatic ash conveyer is arranged on the lower part of the gas low-pressure pulse bag-type duster which is connected with an atomizing cooler; the atomizing cooler is connected with an inlet of a gas draught fan; an outlet of the gas draught fan is respectively connected with a duct butterfly valve and a blind plate valve; the duct butterfly valve is connected with a blow-off valve; the blind plate valve is connected with a gas water seal which is connected with a gasometer; and a small reflux apparatus is respectively arranged on the inlet end and the outlet end of the gas draught fan. The gas dry bag-type purification and recovery device for the converter has the advantages that the gas can meet the national standard requirements.
Description
Technical field;
The invention is the gas fitting that produces when being used to reclaim converter smelting.
Background technology:
Converter produces a large amount of carbon monoxide in smelting process, be commonly called as " coal gas of converter ", and the gasometer of collection " raw gas " contains a large amount of dust, and dust content is up to 20~25g/Nm
3, can not directly use, must carry out could using after the dedusting, the national requirements dust content is at 10g/Nm
3Below could use.At present, reclaim coal gas of converter and mainly adopt two kinds of wet method and dry method.Hydrometallurgic recovery, mainly form by secondary purification device and dewatering unit, the first step adopts sizing or manual setting overflow Venturi meter, its effect is to be the cooling of raw gas and thick dedusting, it is the smart dedusting of raw gas that the excessive unrestrained Venturi meter of automatic path transfer or its effect of employing circumferential weld washer are adopted in the second stage, the dewatering unit effect is the moisture that removes in the piped gas, has a considerable amount of hydrometallurgic recovery device dust concentrations to exceed standard at present.The dry back receiving apparatus mainly is made up of evaporative cooler, electrostatic precipitator and gas cooler etc., and it invests high, and the fault of electric precipitation is many, unloads grey difficulty etc.
Summary of the invention:
The purpose of the invention provides a kind of dry cloth bag purifying recovery device of converter coal gas that dust content in the coal gas of converter that reclaims is up to state standards and requires; The purpose of the invention is to realize by following technical scheme: dry cloth bag purifying recovery device of converter coal gas, it is characterized in that by waste heat boiler, telescopic joint, water-sealed valve, the atomizing cooling tank, pipeline fan, the coal gas Low-Pressure Pulse Bag Filter, the close pneumatic ash conveying plant of full envelope, spray cooler, the coal gas induced draft fan, little reflux, diffuse valve, the pipeline butterfly valve, blank-plate valve, the coal gas water seal, gas chamber is formed, the waste heat boiler outlet connects telescopic joint, the telescopic joint outlet connects water-sealed valve, the water-sealed valve outlet is connected with the import of atomizing cooling tank, the outlet of atomizing cooling tank is connected with the pipeline fan import, the pipeline fan outlet is connected with placed in-line coal gas Low-Pressure Pulse Bag Filter, the close pneumatic ash conveying plant of full envelope is installed in coal gas Low-Pressure Pulse Bag Filter bottom, the coal gas Low-Pressure Pulse Bag Filter connects spray cooler, spray cooler is connected with the import of coal gas induced draft fan, induced draft fan outlet respectively with the pipeline butterfly valve, blank-plate valve connects, the pipeline butterfly valve with diffuse valve and be connected, blank-plate valve is connected with the coal gas water seal, the coal gas water seal is connected with gas chamber, at coal gas induced draft fan entrance end little reflux is installed.
The advantage of the invention: owing to adopted placed in-line coal gas Low-Pressure Pulse Bag Filter, dust removing effects is remarkable, the requirement that is up to state standards of dust content in the coal gas of converter, because the close pneumatic ash conveying plant of full envelope is installed in coal gas Low-Pressure Pulse Bag Filter bottom, reduce environmental pollution, import and export at the coal gas induced draft fan little reflux is installed, control enters pressure, the flow of pipe network, owing to installed and diffused valve, underproof coal gas ignition has been diffused.
Description of drawings:
Fig. 1 is the dry cloth bag purifying recovery device of converter coal gas structural representation.
Among the figure: 1. the close pneumatic ash conveying plant 9. spray coolers 10. coal gas induced draft fans 11. little refluxes 12. of converter 2. waste heat boiler 3. telescopic joints, 4. water-sealed valve 5. atomizing cooling tanks, 6. pipeline fan 7. coal gas Low-Pressure Pulse Bag Filters, 8. full envelopes diffuse valve 13. pipeline butterfly valves 14. blank-plate valve 15. coal gas water seals 16. gas chambers
Embodiment:
Dry cloth bag purifying recovery device of converter coal gas, it is characterized in that by waste heat boiler, telescopic joint, water-sealed valve, the atomizing cooling tank, pipeline fan, the coal gas Low-Pressure Pulse Bag Filter, the close pneumatic ash conveying plant of full envelope, spray cooler, the coal gas induced draft fan, little reflux, diffuse valve, the pipeline butterfly valve, blank-plate valve, the coal gas water seal, gas chamber is formed, the waste heat boiler outlet connects telescopic joint, the telescopic joint outlet connects water-sealed valve, the water-sealed valve outlet is connected with the import of atomizing cooling tank, the outlet of atomizing cooling tank is connected with the pipeline fan import, the pipeline fan outlet is connected with placed in-line coal gas Low-Pressure Pulse Bag Filter, the close pneumatic ash conveying plant of full envelope is installed in coal gas Low-Pressure Pulse Bag Filter bottom, the coal gas Low-Pressure Pulse Bag Filter connects spray cooler, spray cooler is connected with the import of coal gas induced draft fan, induced draft fan outlet respectively with the pipeline butterfly valve, blank-plate valve connects, the pipeline butterfly valve with diffuse valve and be connected, blank-plate valve is connected with the coal gas water seal, the coal gas water seal is connected with gas chamber, at coal gas induced draft fan entrance end little reflux is installed.
Be that waste heat boiler is placed on recyclable coal gas of converter in the converter through pipeline and furnace roof cover during recovery operation, waste heat boiler is cooled to 1350 degree~850 degree with coal gas of converter, pipe laying blower fan between atomizing cooling tank and coal gas Low-Pressure Pulse Bag Filter, make the fire door of converter become negative pressure value, be convenient to smelt, the coal gas Low-Pressure Pulse Bag Filter adopts the off-line type ash cleaning and dust removing device, the atomizing cooling tank continues to be cooled to 250 degree~150 degree with coal gas of converter, the coal gas Low-Pressure Pulse Bag Filter is delivered to the dust of collecting in total grey storehouse through the close pneumatic ash conveying plant of full envelope and is regularly effluxed, can diffuse by diffusing the valve point fire when gas quality is defective, little reflux may command enters the gas pressure and the flow of pipe network.
Claims (1)
1, dry cloth bag purifying recovery device of converter coal gas, it is characterized in that by waste heat boiler, telescopic joint, water-sealed valve, the atomizing cooling tank, pipeline fan, the coal gas Low-Pressure Pulse Bag Filter, the close pneumatic ash conveying plant of full envelope, spray cooler, the coal gas induced draft fan, little reflux, diffuse valve, the pipeline butterfly valve, blank-plate valve, the coal gas water seal, gas chamber is formed, the waste heat boiler outlet connects telescopic joint, the telescopic joint outlet connects water-sealed valve, the water-sealed valve outlet is connected with the import of atomizing cooling tank, the outlet of atomizing cooling tank is connected with the pipeline fan import, the pipeline fan outlet is connected with placed in-line coal gas Low-Pressure Pulse Bag Filter, the close pneumatic ash conveying plant of full envelope is installed in coal gas Low-Pressure Pulse Bag Filter bottom, the coal gas Low-Pressure Pulse Bag Filter connects spray cooler, spray cooler is connected with the import of coal gas induced draft fan, induced draft fan outlet respectively with the pipeline butterfly valve, blank-plate valve connects, the pipeline butterfly valve with diffuse valve and be connected, blank-plate valve is connected with the coal gas water seal, the coal gas water seal is connected with gas chamber, at coal gas induced draft fan entrance end little reflux is installed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CNU2008200117890U CN201169596Y (en) | 2008-03-28 | 2008-03-28 | Revolving furnace coal gas dry method cloth bag purification recovering device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CNU2008200117890U CN201169596Y (en) | 2008-03-28 | 2008-03-28 | Revolving furnace coal gas dry method cloth bag purification recovering device |
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CN201169596Y true CN201169596Y (en) | 2008-12-24 |
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CNU2008200117890U Expired - Lifetime CN201169596Y (en) | 2008-03-28 | 2008-03-28 | Revolving furnace coal gas dry method cloth bag purification recovering device |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101892089A (en) * | 2010-08-04 | 2010-11-24 | 中冶京诚工程技术有限公司 | Electric furnace gas purification and reclamation equipment |
CN102344987A (en) * | 2011-10-31 | 2012-02-08 | 中冶南方工程技术有限公司 | Primary flue gas dry dedusting process for vanadium recovering converter |
CN117327863A (en) * | 2023-10-11 | 2024-01-02 | 陕西西北风机制造有限公司 | Cooling and dedusting device of primary dedusting fan of converter |
-
2008
- 2008-03-28 CN CNU2008200117890U patent/CN201169596Y/en not_active Expired - Lifetime
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101892089A (en) * | 2010-08-04 | 2010-11-24 | 中冶京诚工程技术有限公司 | Electric furnace gas purification and reclamation equipment |
CN101892089B (en) * | 2010-08-04 | 2013-10-16 | 中冶京诚工程技术有限公司 | Electric furnace gas purification and reclamation equipment |
CN102344987A (en) * | 2011-10-31 | 2012-02-08 | 中冶南方工程技术有限公司 | Primary flue gas dry dedusting process for vanadium recovering converter |
CN102344987B (en) * | 2011-10-31 | 2013-09-18 | 中冶南方工程技术有限公司 | Primary flue gas dry dedusting process for vanadium recovering converter |
CN117327863A (en) * | 2023-10-11 | 2024-01-02 | 陕西西北风机制造有限公司 | Cooling and dedusting device of primary dedusting fan of converter |
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Granted publication date: 20081224 |
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CX01 | Expiry of patent term |