CN208349862U - The online drying system of coke - Google Patents

The online drying system of coke Download PDF

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Publication number
CN208349862U
CN208349862U CN201820960737.1U CN201820960737U CN208349862U CN 208349862 U CN208349862 U CN 208349862U CN 201820960737 U CN201820960737 U CN 201820960737U CN 208349862 U CN208349862 U CN 208349862U
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CN
China
Prior art keywords
hot
heat exchanger
air
coke
air duct
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201820960737.1U
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Chinese (zh)
Inventor
张建军
李军
高友
刘振东
孙铭
齐超群
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tangshan Iron and Steel Group Co Ltd
Original Assignee
Tangshan Iron and Steel Group Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tangshan Iron and Steel Group Co Ltd filed Critical Tangshan Iron and Steel Group Co Ltd
Priority to CN201820960737.1U priority Critical patent/CN208349862U/en
Application granted granted Critical
Publication of CN208349862U publication Critical patent/CN208349862U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

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  • Coke Industry (AREA)

Abstract

The utility model relates to coke manufacturing equipment, specifically a kind of online drying system of coke.Including hot-blast stove, heat exchanger, air-introduced machine, chimney is emptied, coke feed bin, heat exchanger includes heat exchanger flue gas disposed in parallel end and heat exchanger air end, the side at heat exchanger flue gas end is connected to by flue with hot-blast stove, and the other side at heat exchanger flue gas end is connected to by exhaust piping with waste stack;The side of heat exchanger air end is connected to by cold-air duct with air-introduced machine, the other side of heat exchanger air end is connected to one end of the first hot-air duct, the other end of first hot-air duct is connected to the head end of the second hot-air duct in coke feed bin, and the end of the second hot-air duct is connected to emptying chimney.The utility model solves the problems, such as that coke moisture is high, and coke moisture content reduces 1% ~ 2%, improves screening efficiency, stablizes in-furnace temperature, reduces ton iron production cost.

Description

The online drying system of coke
Technical field
The utility model relates to coke manufacturing equipment, specifically a kind of online drying system of coke.
Background technique
Coke is that one of the important source material that blast furnace ironmaking uses due to being influenced by environmental factors such as rainwater causes coke There are a large amount of moisture in stacking process for charcoal, while a large amount of aqueous coke enter in blast-furnace coke feed bin.Coke feed bin includes Water coke enters blast-furnace roasting after vibrating screen sieves.But the coke adhered on coke is influenced by moisture in screening process Powder sticks on sieve and coke, and screening effect is bad, meanwhile, feeding density charcoal excess moisture and attachment coke powder increase, and will cause furnace Interior temperature reduces, and fuel ratio increases, and increases ton iron production cost.
Utility model content
The technical problem to be solved by the present invention is to provide a kind of online drying systems of coke, discharge fume using outside hot-blast stove Coke in gas residual heat drying coke feed bin.
The utility model solve its technical problem the technical solution adopted is that:
A kind of online drying system of coke, including hot-blast stove, heat exchanger, air-introduced machine empty chimney, coke feed bin, heat exchange Device includes heat exchanger flue gas disposed in parallel end and heat exchanger air end, and the side at heat exchanger flue gas end passes through flue and heat The other side of wind furnace connection, heat exchanger flue gas end is connected to by exhaust piping with waste stack;The side of heat exchanger air end is logical Supercooled air pipeline is connected to air-introduced machine, and the other side of heat exchanger air end is connected to one end of the first hot-air duct, and first The other end of hot-air duct is connected to the head end of the second hot-air duct in coke feed bin, the end of the second hot-air duct It is connected to emptying chimney.
The utility model by adopting the above technical scheme, compared with prior art, beneficial effect is:
Solve the problems, such as that coke moisture is high, coke moisture content reduces 1% ~ 2%, improves screening efficiency, stablizes in furnace Temperature reduces ton iron production cost.
Further, the prioritization scheme of the utility model is:
Flue is oppositely arranged with cold-air duct.
Exhaust piping is oppositely arranged with the first hot-air duct.
The end of first hot-air duct is equipped with regulating valve.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model embodiment;
In figure: hot-blast stove 1;Flue 2;Heat exchanger 3;Heat exchanger flue gas end 4;Exhaust piping 5;Waste stack 6;Air inducing Machine 7;Cold-air duct 8;Heat exchanger air end 9;First hot-air duct 10;Empty chimney 11;Coke feed bin 12;Regulating valve 13;Second hot-air duct 14.
Specific embodiment
The utility model is further illustrated with reference to the accompanying drawings and examples.
Refering to fig. 1, the online drying system of a kind of coke by hot-blast stove 1, flue 2, heat exchanger 3, exhaust piping 5, is given up Gas chimney 6, air-introduced machine 7, cold-air duct 8, the first hot-air duct 10, emptying chimney 11, coke feed bin 12,13 and of regulating valve Second hot-air duct 14 is constituted.
Heat exchanger 3 is made of heat exchanger flue gas end 4 and heat exchanger air end 9, heat exchanger flue gas end 4 and heat exchanger air end About 9 are arranged in parallel, and the side at hot device flue gas end 4 is connected to by flue 2 with the bottom of hot-blast stove 1, hot device flue gas end 4 The other side is connected to by exhaust piping 5 with the bottom of waste stack 6.Realize the residual temperature flue gas of the discharge of hot-blast stove 1 via fume pipe Road 2, heat exchanger flue gas end 4, exhaust piping 5,6 outlet of waste stack.
The side of heat exchanger air end 9 is connected to by cold-air duct 8 with the air outlet of air-introduced machine 7, heat exchanger air end 9 The other side be connected to one end of the first hot-air duct 10, in the other end of the first hot-air duct 10 and coke feed bin 12 The head end of second hot-air duct 14 is connected to, and the end of the second hot-air duct 14 is connected to emptying chimney 11, the first hot-air The end of pipeline 10 is equipped with regulating valve 13.
Cold air is introduced after cold-air duct 8 via air-introduced machine 7 and is being changed into heat exchanger air end 9, cold air and flue gas It exchanges heat in hot device 3, the hot-air after heat exchange enters the second heat sky in coke feed bin 12 by the first hot-air duct 10 Feed channel 14 exchanges heat, and realizes coke moisture drying, and the hot-air after heat exchange is discharged by emptying chimney 11.
Flue 2 is oppositely arranged with cold-air duct 8, and exhaust piping 5 is oppositely arranged with the first hot-air duct 10.It is real The flow direction of existing cold air and flue gas is on the contrary, increase heat transfer effect.
The present embodiment controls hot air flowrate using regulating valve 13, guarantees that 12 coke of coke feed bin is normally dried, prevents heat Air mass flow is excessive to cause drying is excessive the generation of coke fragmentation phenomenon occur.
Due to, containing a large amount of remaining coal gas, existing so that directly drying coke using hot-blast stove fume in hot-blast stove fume Security risk, so the utility model carries out flue gas and air heat-exchange using heat exchanger, so that into the hot-air of coke feed bin Without excessive gas composition, guarantees the safety of production district, eliminate safe hidden trouble.
The above is only the preferred feasible embodiment of the utility model, not thereby limits to the power of the utility model Sharp range, it is all with equivalence changes made by the utility model specification and its accompanying drawing content, it is both contained in right of the invention Within the scope of.

Claims (4)

1. a kind of online drying system of coke, including hot-blast stove, heat exchanger, air-introduced machine empty chimney, coke feed bin, feature Be: heat exchanger includes heat exchanger flue gas disposed in parallel end and heat exchanger air end, and the side at heat exchanger flue gas end passes through cigarette Feed channel is connected to hot-blast stove, and the other side at hot device flue gas end is connected to by exhaust piping with waste stack;Heat exchanger air end Side be connected to air-introduced machine by cold-air duct, one end company of the other side of heat exchanger air end and the first hot-air duct Logical, the other end of the first hot-air duct is connected to the head end of the second hot-air duct in coke feed bin, the second warm-air pipe The end in road is connected to emptying chimney.
2. the online drying system of coke according to claim 1, it is characterised in that: flue is opposite with cold-air duct Setting.
3. the online drying system of coke according to claim 1, it is characterised in that: exhaust piping and the first hot-air duct It is oppositely arranged.
4. the online drying system of coke according to claim 1, it is characterised in that: install the end of the first hot-air duct There is regulating valve.
CN201820960737.1U 2018-06-21 2018-06-21 The online drying system of coke Expired - Fee Related CN208349862U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820960737.1U CN208349862U (en) 2018-06-21 2018-06-21 The online drying system of coke

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820960737.1U CN208349862U (en) 2018-06-21 2018-06-21 The online drying system of coke

Publications (1)

Publication Number Publication Date
CN208349862U true CN208349862U (en) 2019-01-08

Family

ID=64880594

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201820960737.1U Expired - Fee Related CN208349862U (en) 2018-06-21 2018-06-21 The online drying system of coke

Country Status (1)

Country Link
CN (1) CN208349862U (en)

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GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20190108

Termination date: 20200621

CF01 Termination of patent right due to non-payment of annual fee