CN208604143U - A kind of dynamic regulation oxygen-enriched air blast richness CO2The control system of rate - Google Patents

A kind of dynamic regulation oxygen-enriched air blast richness CO2The control system of rate Download PDF

Info

Publication number
CN208604143U
CN208604143U CN201821089204.7U CN201821089204U CN208604143U CN 208604143 U CN208604143 U CN 208604143U CN 201821089204 U CN201821089204 U CN 201821089204U CN 208604143 U CN208604143 U CN 208604143U
Authority
CN
China
Prior art keywords
control unit
oxygen
richness
flow
rate
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.)
Active
Application number
CN201821089204.7U
Other languages
Chinese (zh)
Inventor
朱荣
武文合
董凯
陈培敦
吕明
胡绍岩
韩宝臣
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.)
University of Science and Technology Beijing USTB
Shandong Taishan Steel Group
Original Assignee
University of Science and Technology Beijing USTB
Shandong Taishan Steel Group
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 University of Science and Technology Beijing USTB, Shandong Taishan Steel Group filed Critical University of Science and Technology Beijing USTB
Priority to CN201821089204.7U priority Critical patent/CN208604143U/en
Application granted granted Critical
Publication of CN208604143U publication Critical patent/CN208604143U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • Y02P10/20Recycling

Landscapes

  • Manufacture Of Iron (AREA)

Abstract

The utility model belongs to blast furnace ironmaking green high-efficient production field, and in particular to a kind of dynamic regulation oxygen-enriched air blast richness CO2The control system of rate, the control system can real-time dynamic regulation oxygen-enriched air blast richness CO2Rate realizes oxygen enrichment percentage and richness CO in oxygen-enriched air blast2The optimization matching of rate controls air port ignition temperature in zone of reasonableness, and air port ignition temperature is excessively high caused by solving the problems, such as because of raising blast furnace air oxygen enrichment percentage, further increases yield for blast furnace and provides solution, also achieves CO2In the recycling application of blast furnace ironmaking process.

Description

A kind of dynamic regulation oxygen-enriched air blast richness CO2The control system of rate
Technical field
The utility model belongs to blast furnace ironmaking green high-efficient production field, and in particular to a kind of dynamic regulation oxygen-enriched air blast is rich CO2The control system of rate.
Background technique
Cupola well Warm status has a major impact smooth operation of furnace and molten steel quality, in production practice of blast furnace, usually by air port Raceway zone ignition temperature is as the important reference indicator for measuring cupola well Warm status.A large amount of production practices show to maintain blast furnace Normal operating conditions, Tuyere Raceway ignition temperature should be stablized in reasonable interval.Tuyere Raceway ignition temperature is too low, air port The fuel combustion of blowing is insufficient, furnace charge underheat, causes reduction of iron ore insufficient, slag iron temperature is low;Temperature is excessively high, SiO A large amount of gasifications, coal gas rapid spatial expansion cause furnace charge decline resistance to increase, influence smooth operation of furnace, while localized hyperthermia causes Strong heat radiation accelerate the erosion of cupola well refractory material, make safety in production hidden danger of the blast furnace there are hearth breakout.
The mode of intensification of smelting process in BF is oxygen-enriched air blast at present, i.e., industrial oxygen is added in blast-furnace hot-air, improves air blast Oxygen enrichment percentage, enhanced fuel improve rate of driving in Tuyere Raceway burning degree, increase furnace processor, but excessively high oxygen enrichment percentage Will lead to air port ignition temperature transfinites, and limits the further promotion of oxygen enrichment percentage, therefore how to further increase oxygen-enriched in hot wind Rate is the main difficult technical that ironmaking worker faces.There is scholar to propose that CO is added in blast-furnace hot-air2Gas utilizes CO2Gas With the characteristic of carbon endothermic heat of reaction in Tuyere Raceway coal dust, coke, solve hot wind in oxygen concentration it is excessively high cause air port return Revolve the excessively high problem of area's ignition temperature.
But in State of Blast Furnace it is a high temperature and pressure multiphase system, and in actual production process, each operating parameter in State of Blast Furnace As coke ingredient, coal dust ingredient, pig iron ingredient, the blow rate required, hot blast temperature, blast humidity fluctuate larger, and nothing with smelting process Method real-time detection, static Tuyere Raceway theoretical temperature combustion computation model can not obtain oxygen-enriched under best air port ignition temperature Rate and richness CO2The rational proportion of rate has seriously affected oxygen-enriched air blast and richness CO in blast furnace air2The cooperation of aeration operation.
Utility model content
To solve the above problems, the utility model proposes a kind of dynamic regulation oxygen-enriched air blast richness CO2The control system of rate.Institute Stating control system can real-time dynamic regulation oxygen-enriched air blast richness CO2Rate realizes oxygen enrichment percentage and richness CO in oxygen-enriched air blast2The optimization of rate Matching is solved by the control of air port ignition temperature in zone of reasonableness because of air port ignition temperature caused by improving blast furnace air oxygen enrichment percentage Excessively high problem further increases yield for blast furnace and provides solution, also achieves CO2In the resource of blast furnace ironmaking process Change application.
The utility model is achieved through the following technical solutions:
A kind of dynamic regulation oxygen-enriched air blast richness CO2The control system of rate, the control system include:
One adjusts and controls in real time the main control unit of the control system;
The temperature measuring unit of one real-time detection In Raceway Before Tuyere of Blast Furnace temperature;
One calculates richness CO in air blast21% richness CO of rate and every increase2The theoretical richness CO of rate air port ignition temperature decreasing value2Rate Computing unit;
One calculates CO2The air blast parameter calculation unit of gas flow and oxygen flow;
One detection and adjusting CO2The CO of flow2Flow monitoring control unit;
One detection and the oxygen flow for adjusting oxygen flow monitor control unit;With
One detection and the hot air flowrate for adjusting hot air flowrate monitor control unit;
The main control unit respectively with the temperature measuring unit, the theoretical richness CO2Rate computing unit and the air blast parameter Computing unit connection;
The air blast parameter calculation unit respectively with the CO2Flow monitoring control unit, oxygen flow monitoring control Unit processed is connected with hot air flowrate monitoring control unit;
Through the CO2Flow monitoring control unit, oxygen flow monitoring control unit and hot air flowrate prison Survey the CO that control unit is sent out2The Tuyere Raceway is sent into after gas, oxygen and hot-air mixing.
Further, Tuyere Raceway abbreviation air port.
Further, the CO2Flow monitoring control unit includes the first decompression balancing device, the adjusting of the first Electromagnetic Flow Valve, the first mass flow sensor and first check-valve;
It is described first decompression balancing device, the first Electromagnetic Flow regulating valve, first mass flow sensor and The first check-valve is sequentially connected, and the first decompression balancing device is arranged in the CO2Flow monitoring control unit into Port, the first check-valve are placed in the CO2The gas outlet of flow monitoring control unit.
Further, the oxygen flow monitoring control unit includes the second decompression balancing device, the second Electromagnetic Flow tune Save valve, the second mass flow sensor and second check-valve;
It is described second decompression balancing device, the second Electromagnetic Flow regulating valve, second mass flow sensor and The second check-valve is sequentially connected, the second decompression balancing device be arranged in oxygen flow monitoring control unit into Port, the second check-valve are placed in the gas outlet of oxygen flow monitoring control unit.
Further, the hot air flowrate monitoring control unit includes third decompression balancing device, third Electromagnetic Flow Regulating valve, third mass flow sensor and third check-valves;
Third decompression balancing device, the third Electromagnetic Flow regulating valve, the third mass flow sensor and The third check-valves is sequentially connected, and the hot air flowrate monitoring control unit is arranged in the third decompression balancing device Air inlet, the third check-valves are placed in the gas outlet of hot air flowrate monitoring control unit.
Further, the dynamic regulation oxygen-enriched air blast richness CO2The control system of rate further includes a blasting unit, the drum Wind unit is arranged in the CO2Flow monitoring control unit, oxygen flow monitoring control unit and the hot air flowrate The gas outlet for monitoring control unit, for making CO2Gas, oxygen and hot-air are sent into the Tuyere Raceway after being sufficiently mixed.
Further, the blasting unit includes one for the surge tank of gas buffer and the gas of a detection gas flow Flow sensor, the surge tank are connect with the gas flow sensor.
Further, the temperature measuring unit is Non-contacting Infrared Thermometer;The biography of the Non-contacting Infrared Thermometer Sensor is set to blast branch pipe of blast furnace blow-through pipe end peep-hole center.
The utility model has following advantageous effects:
(1) a kind of dynamic regulation oxygen-enriched air blast richness CO of the utility model2The control system of rate, structure is simple, integrated level Height is widely used.
(2) a kind of dynamic regulation oxygen-enriched air blast richness CO of the utility model2The control system of rate utilizes richness CO in air blast2Rate Computation model calculates the rich CO under specific operation2Rate measures air port ignition temperature using temperature measuring unit, operates according to blast furnace process The thinking of Iterative Optimal Control, the blast furnace air richness CO of dynamic adjustment in real time2Rate realizes oxygen enrichment percentage and richness CO in oxygen-enriched blast furnace air2 Rate optimization matching guarantees that Tuyere Raceway ignition temperature is stablized in reasonable interval while further increasing furnace processor, Cupola well normal operating conditions is maintained, while also achieving blast furnace ironmaking process CO2Recycling application.
Detailed description of the invention
Fig. 1 is dynamic regulation oxygen-enriched air blast richness CO in the utility model embodiment 12The structural representation of the control system of rate Figure.
Fig. 2 is that the infrared temperature probe setting position of Non-contacting Infrared Thermometer in the utility model embodiment 1 shows It is intended to.
Fig. 3 is dynamic regulation oxygen-enriched air blast richness CO in the utility model embodiment 22It include air blast list in the control system of rate The schematic diagram of member.
Description of symbols: 1- main control unit;2- temperature measuring unit;3- theory richness CO2Rate computing unit;4- air blast parameter meter Calculate unit;5‐CO2Flow monitoring control unit, 51- first depressurize balancing device, 52- the first Electromagnetic Flow regulating valve, 53- the One mass flow sensor, 54- first check-valve;6- oxygen flow monitors control unit, and 61- second depressurizes balancing device, 62- Second Electromagnetic Flow regulating valve, the second mass flow sensor of 63-, 64- second check-valve;The monitoring control of 7- hot air flowrate Unit, 71- third depressurize balancing device, 72- third Electromagnetic Flow regulating valve, 73- third mass flow sensor, 74- third Check-valves;8- blasting unit, 81- surge tank, 82- gas flow sensor.
Specific embodiment
In order to make the purpose of the utility model, technical solutions and advantages more clearly understood, it with reference to embodiments and says Bright book attached drawing, is explained in further detail the utility model.It should be appreciated that specific embodiment described herein is only used In explaining the utility model, it is not used to limit the utility model.
On the contrary, the utility model cover it is any be defined by the claims do in the spirit and scope of the utility model Substitution, modification, equivalent method and scheme.Further, right below in order to make the public have a better understanding the utility model It is detailed to describe some specific detail sections in the datail description of the utility model.Do not have for a person skilled in the art The utility model can also be understood completely in the description of these detail sections.
Embodiment 1
The present embodiment proposes a kind of dynamic regulation oxygen-enriched air blast richness CO2The control system of rate, the control system include:
One adjusts and controls in real time the main control unit 1 of the control system;
The temperature measuring unit 2 of one real-time detection In Raceway Before Tuyere of Blast Furnace temperature;
One calculates richness CO in air blast21% richness CO of rate and every increase2The theoretical richness CO of rate air port ignition temperature decreasing value2Rate meter Calculate unit 3;
One calculates CO2The air blast parameter calculation unit 4 of gas flow and oxygen flow;
One detection and adjusting CO2The CO of flow2Flow monitoring control unit 5;
One detection and the oxygen flow for adjusting oxygen flow monitor control unit 6;With
One detection and the hot air flowrate for adjusting hot air flowrate monitor control unit 7;
The main control unit 1 respectively with the temperature measuring unit 2, the theoretical richness CO2Rate computing unit 3 and air blast ginseng Number computing unit 4 connects;
The air blast parameter calculation unit 4 respectively with the CO2Flow monitoring control unit 5, oxygen flow monitoring Control unit 6 and hot air flowrate monitoring control unit 7 connect;
Through the CO2Flow monitoring control unit 5, oxygen flow monitoring control unit 6 and the hot air flowrate Monitor the CO that control unit 7 is sent out2The Tuyere Raceway is sent into after gas, oxygen and hot-air mixing.
The CO2Flow monitoring control unit 5 include first decompression balancing device 51, the first Electromagnetic Flow regulating valve 52, First mass flow sensor 53 and first check-valve 54;
The first decompression balancing device 51, the first Electromagnetic Flow regulating valve 52, first mass flow sensing Device 53 and the first check-valve 54 are sequentially connected, and the first decompression balancing device 51 is arranged in the CO2Flow monitoring control The air inlet of unit 5 processed, the first check-valve 54 are placed in the CO2The gas outlet of flow monitoring control unit 5.
Oxygen flow monitoring control unit 6 include the second decompression balancing device 61, the second Electromagnetic Flow regulating valve 62, Second mass flow sensor 63 and second check-valve 64;
The second decompression balancing device 61, the second Electromagnetic Flow regulating valve 62, second mass flow sensing Device 63 and the second check-valve 64 are sequentially connected, and the second decompression setting of balancing device 61 is monitored in the oxygen flow to be controlled The air inlet of unit 6 processed, the second check-valve 64 are placed in the gas outlet of oxygen flow monitoring control unit 6.
The hot air flowrate monitoring control unit 7 includes that third depressurizes balancing device 71, third Electromagnetic Flow regulating valve 72, third mass flow sensor 73 and third check-valves 74;
The third decompression balancing device 71, the third Electromagnetic Flow regulating valve 72, third mass flow sensing Device 73 and the third check-valves 74 are sequentially connected, and third decompression balancing device 71 setting is monitored in the hot air flowrate The air inlet of control unit 7, the third check-valves 74 are placed in the gas outlet of hot air flowrate monitoring control unit 7.
The temperature measuring unit 2 selects Non-contacting Infrared Thermometer;The sensor of the Non-contacting Infrared Thermometer is set It is placed in blowpipe blow-through pipe end peep-hole center.
A kind of dynamic regulation oxygen-enriched air blast richness CO that the present embodiment proposes2The control system of rate utilizes richness CO in air blast2Rate Computation model calculates the rich CO under specific operation2Rate measures air port ignition temperature using temperature measuring unit 2, grasps according to blast furnace process Make the thinking of Iterative Optimal Control, the blast furnace air richness CO of dynamic adjustment in real time2Rate realizes oxygen enrichment percentage and richness in oxygen-enriched blast furnace air CO2Rate optimization matching guarantees that Tuyere Raceway ignition temperature is stablized in Reasonable area while further increasing furnace processor Between, cupola well normal operating conditions is maintained, while also achieving blast furnace ironmaking process CO2Recycling application.
Embodiment 2
A kind of dynamic regulation oxygen-enriched air blast richness CO of the proposition of the present embodiment2The control system of rate and the basic phase of embodiment 1 Together, unlike only:
The dynamic regulation oxygen-enriched air blast richness CO2The control system of rate further includes a blasting unit 8, the blasting unit 8 It is arranged in the CO2Flow monitoring control unit 5, oxygen flow monitoring control unit 6 and hot air flowrate monitoring The gas outlet of control unit 7, for making CO2Gas, oxygen and hot-air are sent into the Tuyere Raceway after being sufficiently mixed.
The blasting unit includes one for the surge tank 81 of gas buffer and the gas flow biography of a detection gas flow Sensor 82, the surge tank 81 are connect with the gas flow sensor 82.

Claims (7)

1. a kind of dynamic regulation oxygen-enriched air blast richness CO2The control system of rate, which is characterized in that the control system includes:
One adjusts and controls in real time the main control unit of the control system;
The temperature measuring unit of one real-time detection In Raceway Before Tuyere of Blast Furnace temperature;
One calculates richness CO in air blast21% richness CO of rate and every increase2The theoretical richness CO of rate air port ignition temperature decreasing value2Rate calculates single Member;
One calculates CO2The air blast parameter calculation unit of gas flow and oxygen flow;
One detection and adjusting CO2The CO of flow2Flow monitoring control unit;
One detection and the oxygen flow for adjusting oxygen flow monitor control unit;With
One detection and the hot air flowrate for adjusting hot air flowrate monitor control unit;
The main control unit respectively with the temperature measuring unit, the theoretical richness CO2Rate computing unit and the air blast parameter calculate single Member connection;
The air blast parameter calculation unit respectively with the CO2Flow monitoring control unit, the oxygen flow monitor control unit It is connected with hot air flowrate monitoring control unit;
Through the CO2Flow monitoring control unit, oxygen flow monitoring control unit and hot air flowrate monitoring control The CO that unit is sent out2The Tuyere Raceway is sent into after gas, oxygen and hot-air mixing.
2. a kind of dynamic regulation oxygen-enriched air blast richness CO according to claim 12The control system of rate, which is characterized in that described CO2Flow monitoring control unit includes the first decompression balancing device, the first Electromagnetic Flow regulating valve, the first mass flow sensor And first check-valve;
The first decompression balancing device, the first Electromagnetic Flow regulating valve, first mass flow sensor and described First check-valve is sequentially connected, and the first decompression balancing device is arranged in the CO2The air inlet of flow monitoring control unit, The first check-valve is placed in the CO2The gas outlet of flow monitoring control unit.
3. a kind of dynamic regulation oxygen-enriched air blast richness CO according to claim 12The control system of rate, which is characterized in that described It includes the second decompression balancing device, the second Electromagnetic Flow regulating valve, the second mass flow sensing that oxygen flow, which monitors control unit, Device and second check-valve;
The second decompression balancing device, the second Electromagnetic Flow regulating valve, second mass flow sensor and described Second check-valve is sequentially connected, and the air inlet of the oxygen flow monitoring control unit is arranged in the second decompression balancing device Mouthful, the second check-valve is placed in the gas outlet of oxygen flow monitoring control unit.
4. a kind of dynamic regulation oxygen-enriched air blast richness CO according to claim 12The control system of rate, which is characterized in that described Hot air flowrate monitoring control unit includes third decompression balancing device, third Electromagnetic Flow regulating valve, third mass flow biography Sensor and third check-valves;
Third decompression balancing device, the third Electromagnetic Flow regulating valve, the third mass flow sensor and described Third check-valves is sequentially connected, and the air inlet of the hot air flowrate monitoring control unit is arranged in the third decompression balancing device Mouthful, the third check-valves is placed in the gas outlet of hot air flowrate monitoring control unit.
5. a kind of dynamic regulation oxygen-enriched air blast richness CO according to claim 12The control system of rate, which is characterized in that described Temperature measuring unit is Non-contacting Infrared Thermometer;The sensor of the Non-contacting Infrared Thermometer is set to blast branch pipe of blast furnace Blow-through pipe end peep-hole center.
6. described in any item a kind of dynamic regulation oxygen-enriched air blast richness CO according to claim 1~52The control system of rate, feature It is, the dynamic regulation oxygen-enriched air blast richness CO2The control system of rate further includes a blasting unit, and the blasting unit setting exists The CO2Flow monitoring control unit, oxygen flow monitoring control unit and the hot air flowrate monitor control unit Gas outlet, for making CO2Gas, oxygen and hot-air are sent into the Tuyere Raceway after being sufficiently mixed.
7. a kind of dynamic regulation oxygen-enriched air blast richness CO according to claim 62The control system of rate, which is characterized in that described Blasting unit includes one for the surge tank of gas buffer and the gas flow sensor of a detection gas flow, the surge tank It is connect with the gas flow sensor.
CN201821089204.7U 2018-07-10 2018-07-10 A kind of dynamic regulation oxygen-enriched air blast richness CO2The control system of rate Active CN208604143U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201821089204.7U CN208604143U (en) 2018-07-10 2018-07-10 A kind of dynamic regulation oxygen-enriched air blast richness CO2The control system of rate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201821089204.7U CN208604143U (en) 2018-07-10 2018-07-10 A kind of dynamic regulation oxygen-enriched air blast richness CO2The control system of rate

Publications (1)

Publication Number Publication Date
CN208604143U true CN208604143U (en) 2019-03-15

Family

ID=65668333

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201821089204.7U Active CN208604143U (en) 2018-07-10 2018-07-10 A kind of dynamic regulation oxygen-enriched air blast richness CO2The control system of rate

Country Status (1)

Country Link
CN (1) CN208604143U (en)

Similar Documents

Publication Publication Date Title
KR101987139B1 (en) Method for detecting air flow distribution in blast furnace
CN108359760A (en) Large blast furnace maintains the operating procedure of direct motion using low-heat state strength coke
CN104480241B (en) A kind of method of the banking fast quick-recovery working of a furnace
CN103468843A (en) Method for producing qualified pig iron from low-grade high-harmful-element lean ores
CN100395352C (en) Hot blast stove burning method
CN109652606B (en) Low-calorific-value molten iron converter smelting method
US2131031A (en) Method of operating blast furnaces
CN208604143U (en) A kind of dynamic regulation oxygen-enriched air blast richness CO2The control system of rate
CN108676948A (en) A kind of dynamic regulation oxygen-enriched air blast richness CO2The control system and control method of rate
US2778018A (en) Method of and apparatus for operating metallurgical furnaces
CN110205419A (en) A kind of calculation method and system of blast furnace addition scrap smelting save the cost
CN210420008U (en) Blast furnace iron notch oxygen enrichment device
GB2628442A (en) Methods for monitoring and predicting energy consumption of production blast furnace (BF) and hydrogen-rich smelting respectively based on Rist operation line
CN204251632U (en) A kind of blast furnace cooling apparatus
CN109811097A (en) A kind of predictor method of BF Design production capacity
CN109022660B (en) A kind of heating furnace heating high hydrogen content reducing gas
CN202390455U (en) Oxygen-enriched balancing device for blast furnace
CN220977102U (en) Iron ore low-carbon agglomeration test system
CN110658228B (en) Pre-reduction sintering cup test device and test method
US3088821A (en) Open hearth steelmaking process
Melcher Use of Natural Gas in an Experimental Blast Furnace
CN214781953U (en) 150 ton converter oxygen rifle nitrogen gas valves
CN118600116A (en) Energy-saving and carbon-reducing method for 1000 cubic meter of blast furnace smelting
CN117167772A (en) Method for baking gas of dynamic oxygen-enriched combustion type iron-mixing furnace
US2290192A (en) Operation of shaft furnaces

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
PP01 Preservation of patent right
PP01 Preservation of patent right

Effective date of registration: 20200730

Granted publication date: 20190315

PD01 Discharge of preservation of patent
PD01 Discharge of preservation of patent

Date of cancellation: 20230730

Granted publication date: 20190315

PP01 Preservation of patent right
PP01 Preservation of patent right

Effective date of registration: 20230730

Granted publication date: 20190315