CN108397784A - Blast furnace gas ignition diffusion system - Google Patents

Blast furnace gas ignition diffusion system Download PDF

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Publication number
CN108397784A
CN108397784A CN201810181299.3A CN201810181299A CN108397784A CN 108397784 A CN108397784 A CN 108397784A CN 201810181299 A CN201810181299 A CN 201810181299A CN 108397784 A CN108397784 A CN 108397784A
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CN
China
Prior art keywords
ignition
high altitude
blast furnace
burning machine
furnace gas
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.)
Pending
Application number
CN201810181299.3A
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Chinese (zh)
Inventor
王爱英
刘志刚
***
张斌辉
贾江梦
刘彩丽
王罗换
王英春
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.)
HEBEI YUJIAN ENERGY-SAVING TECHNOLOGY Co Ltd
Original Assignee
HEBEI YUJIAN ENERGY-SAVING TECHNOLOGY 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.)
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Publication date
Application filed by HEBEI YUJIAN ENERGY-SAVING TECHNOLOGY Co Ltd filed Critical HEBEI YUJIAN ENERGY-SAVING TECHNOLOGY Co Ltd
Priority to CN201810181299.3A priority Critical patent/CN108397784A/en
Publication of CN108397784A publication Critical patent/CN108397784A/en
Pending legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • F23G7/08Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases using flares, e.g. in stacks
    • F23G7/085Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases using flares, e.g. in stacks in stacks
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B7/00Blast furnaces
    • C21B7/002Evacuating and treating of exhaust gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • F23G7/07Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases in which combustion takes place in the presence of catalytic material
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2202/00Combustion
    • F23G2202/60Combustion in a catalytic combustion chamber
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2207/00Control
    • F23G2207/10Arrangement of sensing devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2209/00Specific waste
    • F23G2209/14Gaseous waste or fumes

Landscapes

  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Regulation And Control Of Combustion (AREA)

Abstract

The invention discloses a kind of blast furnace gas ignition diffusion systems, including control room, pylon, desorption tube burner and high pressure, and conditioner occurs;Desorption tube burner is set as two, and three sets of high altitude ignition co-burning machines are provided on each desorption tube burner, and catalytic reaction chamber and elevator arc generating device are provided in high altitude ignition co-burning machine, and elevator arc generating device occurs conditioner with high pressure and connect;The bottom of high altitude ignition co-burning machine is provided with air intake and gas entry, and the top of high altitude ignition co-burning machine is higher than the top of desorption tube burner;The head of desorption tube burner, which is closed at high altitude ignition co-burning machine, is provided with flame detecting component;Master controller and computer are provided in control room, computer is connect with master controller, and conditioner occurs with high pressure for master controller and flame detecting component is connect.The configuration of the present invention is simple, reasonable design can substantially reduce investment and the operation expense of blast furnace gas ignition, improve the security reliability of blast furnace gas ignition.

Description

Blast furnace gas ignition diffusion system
Technical field
The present invention relates to the technical field of energy saving and environmental protection of steel industry, is diffused more particularly, to a kind of blast furnace gas ignition and be System.
Background technology
With the continuous enhancing of china's overall national strength, national economy stable development, infrastructure constantly improve, China is As the country of world's output of steel first, while being also that steel consumes big country, pneumatic steelmaking is the important composition portion of steel production Point, a large amount of inflammable, toxic, flammable coal gas of converter and other pollution tail gas, great Liang Yi are will produce in converter production process When combustion, the toxic, gas that is corrosive can not recycle, in order to avoid polluting environment, spreading burner must be set and handle this A little inflammable and explosive or toxic industrial waste gases and tail gas.Blast furnace gas is the byproduct of blast furnace ironmaking, principal combustible composition be CO, H2With a small amount of CH4, there is a large amount of N2And CO2, transmission & distribution are carried out by closed pipe network.But in the actual production process, Due to the production of coal gas and for there are certain lacks of uniformity, would have to implement extra coal gas when pipe network is more than design pressure It diffuses, if the blast furnace gas diffused is directly discharged into air by diffusing tower, serious atmosphere pollution can be caused, influence surrounding Environment, or even personnel's gas poisoning is caused in the particular surroundings of individual periods.
Currently, the traditional way of domestic iron and steel enterprises is to retain ever-burning flame at the top of each diffusing tower, the igniting of ever-burning flame It is usually the coke-stove gas of high heating value with burning air source;No matter whether blast furnace gas diffuses, the ever-burning flame of this burning coke-stove gas Round-the-clock burning in 24 hours in one day.And the impurity contents such as tar are higher in coke-stove gas, it is easy to cause coke oven gas pipe It blocks, with burning fray-out of flame;It is unable to fully burn so that diffusing blast furnace gas, the exceeded accidents of CO occurs.Therefore, these are grown Open fire not only consumes a large amount of high heating value combustion gas of enterprise, and leading to iron and steel enterprise, the production cost increases, and it is unreliable to light a fire, Larger pollution is caused to environment.For these reasons, it is necessary to design a kind of blast furnace gas ignition diffusion system.
Invention content
The object of the present invention is to provide a kind of blast furnace gas ignition diffusion systems, and simple in structure, reasonable design can be significantly Investment and the operation expense for reducing blast furnace gas ignition, improve the security reliability of blast furnace gas ignition.
To achieve the above object, the present invention provides a kind of blast furnace gas ignition diffusion system, including control room, pylon, Conditioner occurs for the desorption tube burner and high pressure being arranged on the pylon;
The desorption tube burner is set as two, and three sets of high altitude ignition cos are provided on each desorption tube burner Burner, catalytic reaction chamber and elevator arc generating device are provided in the high altitude ignition co-burning machine, and the elevator electric arc occurs Device occurs conditioner with the high pressure and is connect by high-tension cable;
The bottom of the high altitude ignition co-burning machine is provided with air intake and gas entry, the high altitude ignition co-burning machine Top is higher than the top of the desorption tube burner;
The head of the desorption tube burner, which is closed at the high altitude ignition co-burning machine, is provided with flame detecting component, described The setting quantity of flame detecting component is consistent with the setting quantity of the high altitude ignition co-burning machine;It is provided with master in the control room Controller and computer, the computer are connect with the master controller, and with the high pressure conditioner occurs for the master controller It is connected with the flame detecting component.
Preferably, the height of the high altitude ignition co-burning machine is 1.3 meters, and the top of the high altitude ignition co-burning machine is higher than 0.4 meter of the desorption tube burner top, the desorption tube burner, which is welded with the high altitude ignition co-burning machine by stabilizer blade, to be connected It connects.
Preferably, the high pressure generation conditioner is set as six sets, and on the pylon on number second layer platform, The environment temperature that conditioner occurs for the high pressure is -45~60 DEG C, and working method is controlled interruption or continuous work.
Preferably, the operating temperature of the high altitude ignition co-burning machine is -45~1000 DEG C, and resistance to 1200 DEG C of high temperature impacts, Material is stainless steel.
Preferably, the environment temperature of the flame detecting component is -45~100 DEG C, and detection temperature is 0~1000 DEG C, fire The flame response time is less than 30 seconds.
Preferably, the blast furnace gas that the high altitude ignition co-burning machine uses is introduced in the catalytic reaction chamber, is introduced When flow velocity be 1-30m/s, calorific value >=600kcal/m3
Therefore, the present invention uses above-mentioned blast furnace gas ignition diffusion system, simple in structure, reasonable design that can drop significantly The investment of low blast furnace gas ignition and operation expense improve the security reliability of blast furnace gas ignition.
Below by drawings and examples, technical scheme of the present invention will be described in further detail.
Description of the drawings
Fig. 1 is a kind of work flow diagram of blast furnace gas ignition diffusion system embodiment of the present invention;
Fig. 2 is a kind of structural schematic diagram of blast furnace gas ignition diffusion system embodiment of the present invention.
Specific implementation mode
Embodiment
Fig. 1 is a kind of work flow diagram of blast furnace gas ignition diffusion system embodiment of the present invention, and Fig. 2 is that the present invention is a kind of The structural schematic diagram of blast furnace gas ignition diffusion system embodiment, as shown, the present invention provides a kind of blast furnace gas ignitions Conditioner 4 occurs for diffusion system, including control room 1, pylon 2, the desorption tube burner 3 being arranged on pylon 2 and high pressure;It diffuses Pipe burner 3 is set as two, and three sets of high altitude ignition co-burning machines 5, high altitude ignition co-burning are provided on each desorption tube burner 3 Catalytic reaction chamber 6 and elevator arc generating device 7 are provided in device 5, with high pressure conditioner 4 occurs for elevator arc generating device 7 It is connected by high-tension cable;The bottom of high altitude ignition co-burning machine 5 is provided with air intake 8 and gas entry 9, high altitude ignition co-burning The top of device 5 is higher than the top of desorption tube burner 3;The head of desorption tube burner 3, which is closed at high altitude ignition co-burning machine 5, to be arranged There are flame detecting component 10, the setting quantity of flame detecting component 10 consistent with the setting quantity of high altitude ignition co-burning machine 5;Control Master controller 11 and computer 12 are provided in room 1, computer 12 is connect with master controller 11, and master controller 11 occurs with high pressure Conditioner 4 and flame detecting component 10 connect, the present invention be when desorption tube burner will diffused gas when, and fired in desorption tube Burner is lighted always during diffusing, and the elevator arc generating device in high altitude ignition co-burning machine stops work after ignition Make, no longer consumes electric energy, the combustion case of desorption tube burner has corresponding flame detecting component, it is ensured that is put when diffusing combustion gas Separate tube burner is in completely burned state, the igniting of high altitude ignition co-burning machine and does not need other any fuel gas with burning, only It is just to be used when desorption tube burner diffuses, is greatly reduced with the cost for combusting gas, zero consumption of processing is diffused in pursuit, is The design of system from light automatically, with burnings, flame monitoring, the software and hardware technology of control system and equipment all using current control field Advanced technology, while having fully considered the safety and reliability of application, using by practice test for many years and continuously improving Ripe equipment and technology.
The course of work of system is:
After master controller obtains starting ignition signal, start corresponding direct-fired high altitude ignition co-burning machine igniting, peace immediately The flame detecting component moment by desorption tube burner monitors flame conditions, after high altitude ignition co-burning machine is lighted, high-altitude Ignition section in point partner's burner is stopped, and high altitude ignition co-burning machine is changed into high-altitude with burner, and high-altitude continues with burner It lights until desorption tube burner stopping is diffused.
The course of work of high altitude ignition co-burning machine is:
When coal gas main pipe pressure, which reaches design, diffuses value, after master controller obtains starting ignition signal, occur to high pressure Conditioner feeds 220V alternating currents, and high pressure occurs the high-voltage electricity that conditioner generates and gives high altitude ignition co-burning machine by high-tension cable Interior elevator arc generating device generates planar electric arc, while the blast furnace gas that desorption tube burner diffuses is introduced into directly automatically Inside combustion high altitude ignition co-burning machine, it is ignited in the case where being catalyzed reagentia, jets out flames from high altitude ignition co-burning machine top, it is high Null point partner burner, flame detecting component are mounted on desorption tube burner head, and high pressure occurs conditioner and is mounted on pylon platform On, by main controller controls, master controller is the highly reliable intelligent control system with compositions such as PLC and input and output, it is high The control core of producer gas ignition bleeding system, it implements comprehensive management to field device and carries out data acquisition, while will letter Breath is transmitted to computer, can also carry out semi-automatic, skilled hand at the scene and move ignition operation, and the information of live main controller passes through remote Transmission unit and communication cable are sent on the computer of master control room, on computers it is observed that the work at scene Process, flame conditions, logout and various tendency charts and the variation of each parameter, while ignition operation, modification parameter can be carried out Deng.
The height of high altitude ignition co-burning machine 5 is 1.3 meters, and the top of high altitude ignition co-burning machine 5 is higher than desorption tube burner 3 0.4 meter of top, desorption tube burner 3 is welded to connect with high altitude ignition co-burning machine 5 by stabilizer blade.High pressure occurs conditioner 4 and is arranged It it is six sets, and on pylon 2 on number second layer platform, the environment temperature that conditioner 4 occurs for high pressure is -45~60 DEG C, work It is controlled interruption or continuous work to make mode.
The operating temperature of high altitude ignition co-burning machine 5 is -45~1000 DEG C, and resistance to 1200 DEG C of high temperature impacts, and material is stainless Steel.
The environment temperature of flame detecting component 10 is -45~100 DEG C, and detection temperature is 0~1000 DEG C, the flame response time Less than 30 seconds.
The blast furnace gas that high altitude ignition co-burning machine 5 uses is introduced in catalytic reaction chamber 6, and flow velocity when introducing is 1- 30m/s, calorific value >=600kcal/m3.
Therefore, the present invention uses above-mentioned blast furnace gas ignition diffusion system, simple in structure, reasonable design that can drop significantly The investment of low blast furnace gas ignition and operation expense improve the security reliability of blast furnace gas ignition.
Finally it should be noted that:The above embodiments are merely illustrative of the technical solutions of the present invention rather than is limited, Although the present invention is described in detail with reference to preferred embodiments, it will be understood by those of ordinary skill in the art that:Its according to Technical scheme of the present invention can be so modified or replaced equivalently, and these modifications or equivalent replacement cannot also make to repair Technical solution after changing is detached from the spirit and scope of technical solution of the present invention.

Claims (6)

1. a kind of blast furnace gas ignition diffusion system, it is characterised in that:
Conditioner occurs including control room, pylon, the desorption tube burner being arranged on the pylon and high pressure;
The desorption tube burner is set as two, and three sets of high altitude ignition co-burnings are provided on each desorption tube burner Device is provided with catalytic reaction chamber and elevator arc generating device in the high altitude ignition co-burning machine, and the elevator electric arc fills It sets and is connect by high-tension cable with high pressure generation conditioner;
The bottom of the high altitude ignition co-burning machine is provided with air intake and gas entry, the top of the high altitude ignition co-burning machine Higher than the top of the desorption tube burner;
The head of the desorption tube burner, which is closed at the high altitude ignition co-burning machine, is provided with flame detecting component, the flame The setting quantity of probe assembly is consistent with the setting quantity of the high altitude ignition co-burning machine;
Master controller and computer are provided in the control room, the computer is connect with the master controller, the master control Conditioner occurs with the high pressure for device processed and the flame detecting component is connect.
2. blast furnace gas ignition diffusion system according to claim 1, it is characterised in that:The high altitude ignition co-burning machine Height is 1.3 meters, and the top of the high altitude ignition co-burning machine is higher than 0.4 meter of the desorption tube burner top, described to diffuse Pipe burner is welded to connect with the high altitude ignition co-burning machine by stabilizer blade.
3. blast furnace gas ignition diffusion system according to claim 2, it is characterised in that:The high pressure occurs conditioner and sets It is set to six sets, and on the pylon on number second layer platforms, the environment temperature that conditioner occurs for the high pressure is -45~ 60 DEG C, working method is controlled interruption or continuous work.
4. blast furnace gas ignition diffusion system according to claim 3, it is characterised in that:The high altitude ignition co-burning machine Operating temperature is -45~1000 DEG C, and resistance to 1200 DEG C of high temperature impacts, and material is stainless steel.
5. blast furnace gas ignition diffusion system according to claim 4, it is characterised in that:The ring of the flame detecting component Border temperature is -45~100 DEG C, and detection temperature is 0~1000 DEG C, and the flame response time is less than 30 seconds.
6. blast furnace gas ignition diffusion system according to claim 5, it is characterised in that:The high altitude ignition co-burning machine makes Blast furnace gas is introduced in the catalytic reaction chamber, and flow velocity when introducing is 1-30m/s, calorific value >=600kcal/m3
CN201810181299.3A 2018-03-06 2018-03-06 Blast furnace gas ignition diffusion system Pending CN108397784A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810181299.3A CN108397784A (en) 2018-03-06 2018-03-06 Blast furnace gas ignition diffusion system

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CN201810181299.3A CN108397784A (en) 2018-03-06 2018-03-06 Blast furnace gas ignition diffusion system

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CN108397784A true CN108397784A (en) 2018-08-14

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111500816A (en) * 2020-06-03 2020-08-07 广东韶钢松山股份有限公司 Converter gas ignition and diffusion method and converter gas ignition and diffusion control system

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202131322U (en) * 2011-05-23 2012-02-01 启东市海信机械有限公司 Novel diffusing and automatic ignition system for blast furnace gas
CN203927952U (en) * 2014-06-11 2014-11-05 鞍钢股份有限公司 Automatic ignition and combustion accompanying device for blast furnace gas diffusion
CN104946833A (en) * 2015-07-13 2015-09-30 河北煜剑节能技术有限公司 Automatic ignition and combustion accompanying device for blast furnace and converter gas desorption tower
CN105219900A (en) * 2014-06-11 2016-01-06 鞍钢股份有限公司 Blast furnace gas diffusing method and automatic control system

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202131322U (en) * 2011-05-23 2012-02-01 启东市海信机械有限公司 Novel diffusing and automatic ignition system for blast furnace gas
CN203927952U (en) * 2014-06-11 2014-11-05 鞍钢股份有限公司 Automatic ignition and combustion accompanying device for blast furnace gas diffusion
CN105219900A (en) * 2014-06-11 2016-01-06 鞍钢股份有限公司 Blast furnace gas diffusing method and automatic control system
CN104946833A (en) * 2015-07-13 2015-09-30 河北煜剑节能技术有限公司 Automatic ignition and combustion accompanying device for blast furnace and converter gas desorption tower

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111500816A (en) * 2020-06-03 2020-08-07 广东韶钢松山股份有限公司 Converter gas ignition and diffusion method and converter gas ignition and diffusion control system

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