CN113790607A - Oxygen-enriched combustion system for steel rolling heating furnace and heat treatment furnace and control method - Google Patents
Oxygen-enriched combustion system for steel rolling heating furnace and heat treatment furnace and control method Download PDFInfo
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- CN113790607A CN113790607A CN202111131032.1A CN202111131032A CN113790607A CN 113790607 A CN113790607 A CN 113790607A CN 202111131032 A CN202111131032 A CN 202111131032A CN 113790607 A CN113790607 A CN 113790607A
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D19/00—Arrangements of controlling devices
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N1/00—Regulating fuel supply
- F23N1/02—Regulating fuel supply conjointly with air supply
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N5/00—Systems for controlling combustion
- F23N5/02—Systems for controlling combustion using devices responsive to thermal changes or to thermal expansion of a medium
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D19/00—Arrangements of controlling devices
- F27D2019/0006—Monitoring the characteristics (composition, quantities, temperature, pressure) of at least one of the gases of the kiln atmosphere and using it as a controlling value
- F27D2019/0018—Monitoring the temperature of the atmosphere of the kiln
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D19/00—Arrangements of controlling devices
- F27D2019/0028—Regulation
- F27D2019/0034—Regulation through control of a heating quantity such as fuel, oxidant or intensity of current
- F27D2019/004—Fuel quantity
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D19/00—Arrangements of controlling devices
- F27D2019/0028—Regulation
- F27D2019/0034—Regulation through control of a heating quantity such as fuel, oxidant or intensity of current
- F27D2019/004—Fuel quantity
- F27D2019/0043—Amount of air or O2 to the burner
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Abstract
An oxygen-enriched combustion system for a steel rolling heating furnace and a heat treatment furnace and a control method thereof belong to the technical field of industrial furnaces. The invention further improves the heat efficiency of the steel rolling heating furnace and the heat treatment furnace, reduces the fuel consumption and the pollutant discharge, improves the heating and heat treatment capability, and achieves the purposes of energy conservation, emission reduction, quality improvement and efficiency improvement. When a heating furnace or a heat treatment furnace is normally produced and before the heating furnace or the heat treatment furnace is put into an oxygen-enriched combustion system in advance, a stop valve of an oxygen pipeline for the heating furnace in a plant area is manually opened, the oxygen pressure of the network in the plant area is reduced by 0.3-0.4MPa from 1.4-1.6MPa by controlling a pressure regulating valve, then the oxygen pressure is regulated to 0.11-0.12MPa by a pressure and flow regulating valve, oxygen is doped into a combustion-supporting cold air pipeline of the steel rolling heating furnace and the heat treatment furnace, and the mixed oxygen-enriched air is preheated by an air preheater and then is sent to a nozzle of each control section of the heating furnace or the heat treatment furnace for combustion. The invention has the advantages of simple and safe system configuration, convenient and reliable operation and wide market popularization prospect.
Description
Technical Field
The invention belongs to the technical field of industrial furnaces, and particularly relates to an oxygen-enriched combustion system for a steel rolling heating furnace and a heat treatment furnace and a control method. The main functions of the system are used for a combustion system of a heating furnace and a heat treatment furnace, and the system is used for improving the radiation heat supply coefficient in the furnace, shortening the heating time, improving the heating efficiency and the yield, reducing the fuel consumption, and assisting the energy conservation, emission reduction, quality improvement and efficiency improvement of a steel rolling heating furnace and the heat treatment furnace.
Background
Oxycombustion refers to combustion when the volume fraction of oxygen in the gas supplied for combustion is >2 l%. At present, the combustion-supporting air of the combustion systems of steel rolling heating furnaces and heat treatment furnaces at home and abroad generally adopts conventional air, the oxygen content in the air is 21 percent, the nitrogen is 78 percent, only oxygen accounting for about 21 percent of the total air is involved in combustion in the combustion process, and the nitrogen accounting for 78 percent of the total air and other inert gases are not combustion-supporting but are discharged to the atmosphere along with flue gas to take away a large amount of heat. If oxygen-enriched combustion is adopted, every 1% of oxygen in the combustion air is increased, 4% of nitrogen is correspondingly reduced. Therefore, the oxygen-enriched combustion can accelerate the combustion speed, improve the combustion efficiency, reduce the waste gas amount and have obvious energy-saving and emission-reducing effects. In recent years, heat engineering technicians at home and abroad develop waste heat recovery technologies such as different types of high-efficiency preheaters, heat accumulators and the like, and have good effects of energy conservation, emission reduction, quality improvement and efficiency improvement on steel rolling heating furnaces and heat treatment. However, the technology for improving the thermal efficiency of the heating furnace and the heat treatment furnace has reached a new bottleneck, and it is necessary to develop and apply a new combustion technology to further improve the thermal efficiency of the heating furnace and the heat treatment furnace.
The oxygen-enriched combustion is one of the energy-saving technologies of modern combustion, is called as a resource creative technology by developed countries, is one of the best ways for improving energy efficiency, reducing fuel consumption and reducing pollutant emission for the steel industry with high energy consumption and high pollution, and has a good effect mainly in oxygen-enriched iron making and oxygen-enriched steel making in the domestic and foreign metallurgical industries. Because the oxygen-enriched combustion technology has many advantages of accelerating the combustion speed of fuel, shortening the flame length, improving the flame temperature, reducing the smoke discharge amount, reducing the ignition temperature of the fuel, increasing the heat utilization rate and the like, how to develop and apply the oxygen-enriched combustion technology with high efficiency and low cost to a steel rolling heating furnace and heat treatment is the invention content of the invention.
Disclosure of Invention
The invention aims to provide an oxygen-enriched combustion system for a steel rolling heating furnace and a heat treatment furnace and a control method, which further improve the heat efficiency of the steel rolling heating furnace and the heat treatment furnace, reduce fuel consumption and pollutant discharge, improve heating and heat treatment capacity and achieve the purposes of energy conservation, emission reduction, quality improvement and efficiency improvement.
The utility model provides a be used for steel rolling heating furnace and heat treatment furnace oxygen boosting combustion system includes oxygen pipeline 1, first stop valve 2, oxygen flame arrester 3, oxygen filter 4, pressure regulating valve 5, pressure and flow control valve 6, second stop valve 7, oxygen flame arrester 8, pneumatic quick cut-off valve 9, relief valve 10, oxygen pipeline flowmeter 11, stop check valve 12, cold air pipe 13, air main flowmeter 14, air heater 15, air-blower entry control valve 16, first pressure transmitter 17, second pressure transmitter 18, third pressure transmitter 19, fourth pressure transmitter 20, fifth pressure transmitter 21, first temperature detects 22, second temperature detects 23, third temperature detects 24, oxygen pipeline oxygen analysis appearance 25, hot-air pipeline oxygen analysis appearance 26, furnace flue gas oxygen appearance 27.
Wherein, an oxygen pipeline 1, a first stop valve 2, an oxygen flame arrester 3, an oxygen filter 4, a first pressure transmitter 17, a pressure regulating valve 5, a second pressure transmitter 18, a pressure and flow regulating valve 6, a third pressure transmitter 19, a second stop valve 7, an oxygen flame arrester 8, a pneumatic quick stop valve 9, a safety valve 10, an oxygen pipeline flowmeter 11, a first temperature detection 22, a stop check valve 12 and an oxygen pipeline oxygen analyzer 25 are connected in sequence; the oxygen analyzer 25 is connected with the air main flow meter 14 and the air preheater 15 respectively; a blower inlet adjusting valve 16, a second temperature detector 23, a cold air pipeline 13, a fourth pressure transmitter 20 and an air main flow meter 14 are connected in sequence; the air preheater 15, the third temperature detector 24, the fifth pressure transmitter 21, the hot air pipeline oxygen analyzer 26 and the hearth flue gas oxygen analyzer 27 are connected in sequence.
An oxygen-enriched combustion control method for a steel rolling heating furnace and a heat treatment furnace comprises the following specific steps:
firstly, when a heating furnace or a heat treatment furnace is ignited to start an oxygen-enriched combustion system, starting a heating furnace and a heat treatment furnace blower to perform conventional air supply on the combustion system;
after the gas pipeline of the heating furnace and the heat treatment furnace is blown and diffused to be qualified, starting an ignition program by a combustion control system, and enabling the heating furnace to enter a conventional combustion control mode;
after the heating furnace and the heat treatment furnace enter a conventional combustion control mode, starting an oxygen pipeline control system, opening a plant area oxygen supply heating furnace oxygen pipeline manual valve, and doping oxygen into a cold air main pipeline of the combustion system to improve the concentration of oxygen in combustion air and control an air-fuel ratio and an oxygen-air ratio; the amount of the mixed oxygen is automatically calculated and adjusted by the combustion control system according to the set oxygen-enriched concentration value and the heat load of the heating furnace or the heat treatment furnace;
the air-fuel ratio control method comprises the following steps: according to the components and the heat value of the enterprise gas, when the system is designed, the air-fuel ratio alpha ' of combustion in pure oxygen atmosphere is solved through numerical value, the air-fuel ratio alpha ' is input into a combustion control system as an original parameter, and if the air-fuel ratio alpha is alpha '/21% when the air-fuel ratio alpha is combusted in conventional air; if the fuel is combusted in an atmosphere with an oxygen enrichment rate of x%, the air-fuel ratio α ═ α'/x%;
the oxygen-air ratio control method comprises the following steps: the concentration value n percent detected by the oxygen pipeline oxygen analyzer 26 obtains the oxygen-air ratio (n-x) to (x-0.21) through the oxygen enrichment ratio x percent and the proportion y percent of the conventional air in the oxygen-enriched air;
the combustion control system sets the pressure and the opening degree of the flow regulating valve 6 through the numerical calculation and the actual heat load of the furnace to regulate the actually supplied oxygen amount, and metering, indicating and recording are carried out through an oxygen pipeline flowmeter 11; the amount of the conventional air supplied by the oxygen-enriched combustion system is regulated by a blower inlet regulating valve 16, and is measured, indicated and recorded by an air main flow meter 14; meanwhile, a hot air pipeline oxygen analysis 27 is arranged on the hot air pipeline behind the oxygen mixing point to detect the actual oxygen-enriched concentration after mixing, so as to dynamically correct the oxygen-air ratio value.
The invention has the advantages that the laying of the oxygen pipeline and the oxygen pressure regulating valve station are arranged at the periphery of the blower machine room of the heating furnace or the heat treatment furnace, the environmental temperature is relatively low, and the oxygen pipeline and the oxygen pressure regulating valve station are far away from the radiation high-temperature area around the heating furnace or the heat treatment furnace. Because the oxygen supply system added in the invention is embedded into the existing air and gas combustion system of the heating furnace or the heat treatment furnace, when insufficient oxygen supply occurs in a factory area, the oxygen supply system fails and the heating furnace or the heat treatment furnace fails in operation, the control system automatically cuts off the oxygen supply in a linkage manner, thereby ensuring the safe and reliable operation of the system. The invention has the advantages of simple and safe system configuration, convenient and reliable operation and wide market popularization prospect.
Drawings
FIG. 1 is a schematic view of the oxygen-enriched combustion system and control method of the present invention for a steel rolling heating furnace and a heat treatment furnace. The system comprises an oxygen pipeline 1, a first stop valve 2, an oxygen flame arrester 3, an oxygen filter 4, a pressure regulating valve 5, a pressure and flow regulating valve 6, a second stop valve 7, an oxygen flame arrester 8, a pneumatic quick stop valve 9, a safety valve 10, an oxygen pipeline flowmeter 11, a stop check valve 12, a cold air pipeline 13, an air main flowmeter 14, an air preheater 15, a blower inlet regulating valve 16, a first pressure transmitter 17, a second pressure transmitter 18, a third pressure transmitter 19, a fourth pressure transmitter 20, a fifth pressure transmitter 21, a first temperature detector 22, a second temperature detector 23, a third temperature detector 24, an oxygen pipeline oxygen analyzer 25, a hot air pipeline oxygen analyzer 26 and a hearth flue gas oxygen analyzer 27.
Detailed Description
An oxygen-enriched combustion system for a steel rolling heating furnace and a heat treatment furnace and a control method thereof comprise an oxygen pipeline 1, a first stop valve 2, an oxygen flame arrester 3, an oxygen filter 4, a pressure regulating valve 5, a pressure and flow regulating valve 6, a second stop valve 7, an oxygen flame arrester 8, a pneumatic quick stop valve 9, a safety valve 10, an oxygen pipeline flowmeter 11, a stop check valve 12, a cold air pipeline 13, an air main flowmeter 14, an air preheater 15, a blower inlet regulating valve 16, a first pressure transmitter 17, a second pressure transmitter 18, a third pressure transmitter 19, a fourth pressure transmitter 20, a fifth pressure transmitter 21, a first temperature detector 22, a second temperature detector 23, a third temperature detector 24, an oxygen pipeline oxygen analyzer 25, a hot air pipeline oxygen analyzer 26 and a hearth flue gas oxygen analyzer 27.
When the heating furnace or the heat treatment furnace is normally produced and before the heating furnace or the heat treatment furnace is put into the oxygen-enriched combustion system in advance, the first stop valve 2 and the second stop valve 7 of the oxygen pipeline of the plant area for the heating furnace are manually opened, the control system automatically sets the opening degree of the pressure regulating valve 5, the oxygen pressure of the pipe network of the plant area is reduced by 0.3-0.4MPa from 1.4-1.6MPa, then the pressure and flow regulating valve 6 is used for secondary pressure regulation, the pressure of the oxygen is accurately regulated to 0.11-0.12MPa, the oxygen is mixed into the combustion-supporting cold air pipeline 13 of the steel rolling heating furnace and the heat treatment furnace after the two-stage pressure regulation, and the mixed oxygen-enriched air is preheated by the air preheater 15 and then sent to the front of the nozzles of the control sections of the heating furnace or the heat treatment furnace for mixed combustion in the hearth.
The air-fuel ratio (alpha) and the oxygen-air ratio (beta) are two most key control parameters of the oxygen-enriched combustion system and are also the core content of the invention, and the numerical calculation and control method thereof is as follows:
(1) the air-fuel ratio (alpha) is automatically adjusted. For a combustion system with excellent performance, sufficient combustion of fuel must be ensured, and excessive air cannot be added at the same time, so as to ensure reasonable air-fuel ratio. When oxygen-enriched combustion is adopted, firstly, the air-fuel ratio (alpha') of combustion in pure oxygen atmosphere is determined, and the determination method is as follows:
the method comprises the following steps of firstly, calculating an air-fuel ratio (alpha ') value of combustion in a pure oxygen atmosphere through numerical solution during system design according to the components and the heat value of the enterprise gas, inputting the value into a combustion control computer system as an original parameter, and if the value is combusted in the conventional air, the air-fuel ratio alpha is alpha'/21%.
Secondly, a heat value instrument is arranged on a gas main pipe, the components and heat value data of the gas are detected in real time, a combustion control computer carries out statistical calculation to obtain the air-fuel ratio (alpha') value of the combustion in pure oxygen atmosphere, if the gas is combusted in the conventional air, the air-fuel ratio alpha is equal to the air-fuel ratio alpha
α’/21％。
Therefore, when the fuel is burned in an atmosphere with an oxygen enrichment ratio x% (x% is a process set value), the air-fuel ratio α ═ α'/x% is, for example: calorific value of 8400Kcal/Nm3When natural gas is combusted in a pure oxygen environment, the air-fuel ratio is 2.01:1, and when the natural gas is combusted in oxygen-enriched air with the oxygen-enriched concentration of x%, the air-fuel ratio is 2.01/x%: 1. if the oxygen-enriched concentration is 26 percent: the air-fuel ratio alpha is 2.01/26 percent, 1 is 7.73:1, and the actual oxygen content in the furnace flue gas can be detected by a furnace flue gas oxygen analyzer 27 in the actual production process, so that the air-fuel ratio alpha value is dynamically corrected, and the optimal air-fuel ratio (alpha) control is realized.
(2) The oxygen and air ratio (beta) are automatically adjusted. The oxygen content of the mixed oxygen-enriched air is controlled by adjusting the supply ratio of the oxygen and the combustion-supporting air, so that the oxygen content in the combustion-supporting oxygen-enriched air is ensured to be continuous and stable. Comprehensively considering the economic benefit of the heating furnace or the heat treatment furnace after being put into oxygen-enriched combustion, the oxygen enrichment rate x% is preferably controlled within the range of 22-30%, and the upper limit of the initial oxygen enrichment rate of the combustion system is set to be 30% for control. If the oxygen supplied by the plant pipe network is not 100% pure oxygen, the oxygen supply concentration is detected by setting an oxygen pipeline oxygen analysis 26, and the feedback value of the detected concentration is used for the numerical calculation of the oxygen-air ratio (beta). For example: assuming that the detected value of the supplied concentration is 93%, the blending ratio of oxygen and air is determined based on this, and the specific numerical calculation and control method is as follows:
when the oxygen enrichment rate is x% (the process set value), the proportion of the conventional air in the oxygen-enriched air is y%, and the proportion of the oxygen is z%, then:
x％＝0.21y％+(1-y％)×93％
when the oxygen enrichment ratio is 30%, and y% is 87.5%, the following: 1-87.5% ═ 12.5% oxygen, 87.5% air ratio beta: 12.5 percent;
② when the oxygen enrichment rate is 26%, if y% < 93%: oxygen, z% ═ 1-93% ═ 7%, oxygen, air ratio β = 93%: 7 percent;
③ when the oxygen enrichment rate is 22 percent, y percent is 98.6 percent, then: 1-98.6% ═ 1.4% oxygen, 98.6%: 1.4 percent;
through the above numerical calculation and the actual heat load of the furnace, the combustion control system automatically sets the pressure and the opening of the flow control valve 6 to adjust the amount of oxygen actually supplied, and measures, instructs, and records the amount of oxygen by the oxygen flow meter 11. The amount of air supplied to the oxycombustion system is regulated by a blower inlet regulating valve 16, and is measured, indicated and recorded by an air manifold flow meter 14. Meanwhile, a hot air pipeline oxygen analysis 27 is arranged on a hot air pipeline behind the oxygen mixing point to detect the actual oxygen-enriched concentration after mixing, so as to dynamically correct the oxygen-air ratio (beta) value and ensure the dynamic and accurate control of the whole system.
Oxygen pipeline 1: the pipeline for conveying and supplying to a heating furnace or heat treatment combustion is made of the following materials: 06Cr19Ni10 stainless steel seamless steel pipe.
First and second stop valves 2 and 7: the special stop valve for oxygen is matched with a stainless steel bolt, a nut and a stainless steel polytetrafluoroethylene winding gasket and is used for opening or cutting off oxygen.
Oxygen flame arrestor 3 and oxygen flame arrestor 8: the flame-retardant copper alloy is formed by welding special copper alloy and stainless steel and is respectively arranged behind the first stop valve 2 and the second stop valve 7 to prevent flame from spreading between equipment and pipelines.
The oxygen filter 4: is arranged in front of the pressure regulating valve group and is used for eliminating impurities in the oxygen pipe network so as to protect the normal use of the oxygen pressure regulating valve group.
The pressure regulating valve 5: a pneumatic actuator is configured to reduce the oxygen pressure of a plant pipe network from 1.4-1.6MPa to 0.3-0.4MPa, and primary pressure regulation is carried out;
pressure and flow rate control valve 6: a pneumatic actuator is configured, the pressure of 0.3-0.4MPa after the pressure of the pressure regulating valve 5 is reduced is continuously reduced by 0.11-0.12MPa, secondary pressure regulation and flow regulation are carried out, the pressure after the secondary pressure regulation is higher than the pressure value of 0.01MPa of a cold air main pipe of a combustion system by 0.1MPa, and the requirements of production technology and oxygen safety interlocking control are met;
pneumatic quick trip valve 9: and a pneumatic actuating mechanism is arranged, so that when a combustion system or an oxygen supply system and the like break down, oxygen supply is quickly cut off, and the system safety is ensured.
The safety valve 10: the special oxygen safety valve is adopted and matched with a stainless steel bolt, a nut and a stainless steel polytetrafluoroethylene winding gasket, when the pressure of oxygen supplied is greater than the set value of a system by 0.13MPa after secondary pressure regulation, the safety valve is automatically opened to release pressure, the phenomenon that the pressure of the supplied oxygen is too high is avoided, impact is caused on an air pipeline of a combustion system of a furnace, and the safe operation of the combustion system is ensured.
Oxygen pipeline flow meter 11: the stainless steel orifice plate flowmeter for oxygen, temperature and pressure correction, stainless steel bolt, nut and stainless steel teflon wound gasket are used for detecting, metering and controlling the actual oxygen amount supplied to the furnace for combustion, and the actual oxygen amount is used as the automatic regulating target value and feedback value of oxygen-air ratio (beta).
Stop check valve 12: the oxygen stop check valve is matched with the stainless steel bolt, the nut and the stainless steel polytetrafluoroethylene wound gasket, so that the situation that the pressure of an oxygen pipe network in a factory is too low and the system reflows is avoided, and the safe and stable operation of an oxygen supply system and a combustion system is ensured.
Cold air duct 13: the spiral welded pipe made of Q235 material is used for conveying combustion-supporting air of a heating furnace or a heat treatment furnace, and the mixing point of the oxygen pipeline 1 is arranged on the cold air pipeline 13.
Air manifold flow meter 14: the standard orifice plate is used for flow detection, measurement and control of the actual conventional air quantity supplied to the furnace for combustion, and the conventional air quantity is used as a target value and a feedback value for automatic adjustment of oxygen and air ratio (beta).
The air preheater 15: the mixed oxygen-enriched air is preheated to 400-500 ℃ by adopting a high-efficiency metal tubular heat exchanger, the heat efficiency of the furnace is further improved, and meanwhile, the mixing uniformity of the oxygen and the air is further improved by the twist-shaped cyclone arranged in the 15 tube group of the heat exchanger.
Blower inlet regulating valve 16: and the electric louver valve is used for adjusting the quantity of air for combustion supporting and the pressure of a cold air main pipe.
First pressure transmitter 17: a pressure value for detecting factory oxygen pipe network, metallurgical factory oxygen pipe network pressure value usually: 1.4-16 MPa.
Second pressure transmitter 18: for detecting the value of the oxygen pressure after being depressurized by the pressure regulating valve 5, the normal pressure detection value: 0.3-0.4 MPa.
Third pressure transmitter 19: the pressure value of the oxygen after being reduced by the pressure and flow regulating valve 6 is detected, and the normal pressure detection value is as follows: 0.11-0.12MPa, and meanwhile, the detection value of the third pressure transmitter 19 is used as a pressure value correction signal when the oxygen pipeline flowmeter 11 detects and calculates the flow.
Fourth pressure transmitter 20: the pressure value for detecting the outlet cold air main pipe of the blower is as follows: 0.008-0.01MPa, and the value of 0.1MPa is added to the detection value of the fourth pressure transmitter 20 to be used as the two-stage pressure regulating and controlling target value of the pressure and flow regulating valve 6.
First temperature detection 22: the thermal resistor Pt100 is used for detecting the oxygen temperature of the oxygen pipeline and providing a temperature value correction signal when the oxygen pipeline flow meter 11 detects and calculates the flow.
Second temperature detection 23: the thermal resistor Pt100 is used for detecting the air temperature in the cold air pipeline at the outlet of the blower and providing a temperature value correction signal when the air main flow meter 14 detects and calculates the flow.
Oxygen pipeline oxygen analyzer 25: the laser type oxygen analyzer is adopted to detect the actual oxygen concentration supplied to the heating furnace or the heat treatment furnace, and the actual oxygen concentration is used for calculating the automatic mixing ratio (namely, the oxygen-air ratio beta) of oxygen and air.
Hot air line oxygen analyzer 26: a laser type oxygen analyzer is adopted to detect the actual oxygen concentration in the oxygen-enriched air after the oxygen and the air are mixed, and the actual oxygen concentration is used as a calculation correction value of the automatic mixing ratio (namely the oxygen-air ratio beta) of the oxygen and the air.
Furnace flue gas oxygen analyzer 27: a laser type oxygen analyzer is adopted to detect the actual oxygen concentration in the flue gas in the furnace after the fuel and the oxygen-enriched air are mixed and combusted in the furnace, and the actual oxygen concentration is used as a calculation correction value of the automatic ratio (namely air-fuel ratio alpha) of the oxygen-enriched air and the fuel.
Claims (2)
1. The utility model provides a be used for steel rolling heating furnace and heat treatment furnace oxygen boosting combustion system which characterized in that: the combustion system comprises an oxygen pipeline (1), a first stop valve (2), an oxygen flame arrester (3), an oxygen filter (4), a pressure regulating valve (5), a pressure and flow regulating valve (6), a second stop valve (7), an oxygen flame arrester (8), a pneumatic quick stop valve (9), a safety valve (10), an oxygen pipeline flowmeter (11), a stop check valve (12), a cold air pipeline (13), an air main flowmeter (14), an air preheater (15), a blower inlet regulating valve (16), a first pressure transmitter (17), a second pressure transmitter (18), a third pressure transmitter (19), a fourth pressure transmitter (20), a fifth pressure transmitter (21), a first temperature detector (22), a second temperature detector (23), a third temperature detector (24), an oxygen pipeline oxygen analyzer (25), a hot air pipeline oxygen analyzer (26), A furnace flue gas oxygen analyzer (27);
the oxygen pipeline (1), a first stop valve (2), an oxygen flame arrester (3), an oxygen filter (4), a first pressure transmitter (17), a pressure regulating valve (5), a second pressure transmitter (18), a pressure and flow regulating valve (6), a third pressure transmitter (19), a second stop valve (7), an oxygen flame arrester (8), a pneumatic quick stop valve (9), a safety valve (10), an oxygen pipeline flowmeter (11), a first temperature detection (22), a stop check valve (12) and an oxygen pipeline oxygen analyzer (25) are connected in sequence; the oxygen pipeline oxygen analyzer (25) is respectively connected with the air main flow meter (14) and the air preheater (15); a blower inlet adjusting valve (16), a second temperature detection (23), a cold air pipeline (13), a fourth pressure transmitter (20) and an air main flow meter (14) are connected in sequence; the air preheater (15), the third temperature detector (24), the fifth pressure transmitter (21), the hot air pipeline oxygen analyzer (26) and the hearth flue gas oxygen analyzer (27) are connected in sequence.
2. An oxygen-enriched combustion control method for a steel rolling heating furnace and a heat treatment furnace is characterized in that:
firstly, when a heating furnace or a heat treatment furnace is ignited to start an oxygen-enriched combustion system, starting a heating furnace and a heat treatment furnace blower to perform conventional air supply on the combustion system;
after the gas pipeline of the heating furnace and the heat treatment furnace is blown and diffused to be qualified, starting an ignition program by a combustion control system, and enabling the heating furnace to enter a conventional combustion control mode;
after the heating furnace and the heat treatment furnace enter a conventional combustion control mode, starting an oxygen pipeline control system, opening a plant area oxygen supply heating furnace oxygen pipeline manual valve, and doping oxygen into a cold air main pipeline of the combustion system to improve the concentration of oxygen in combustion air and control an air-fuel ratio and an oxygen-air ratio; the amount of the mixed oxygen is automatically calculated and adjusted by the combustion control system according to the set oxygen-enriched concentration value and the heat load of the heating furnace or the heat treatment furnace;
the air-fuel ratio control method comprises the following steps: according to the components and the heat value of the enterprise gas, when the system is designed, the air-fuel ratio alpha ' of combustion in pure oxygen atmosphere is solved through numerical value, the air-fuel ratio alpha ' is input into a combustion control system as an original parameter, and if the air-fuel ratio alpha is alpha '/21% when the air-fuel ratio alpha is combusted in conventional air; if the fuel is combusted in an atmosphere with an oxygen enrichment rate of x%, the air-fuel ratio α ═ α'/x%;
the oxygen-air ratio control method comprises the following steps: the concentration value detected by an oxygen pipeline oxygen analyzer is n percent, and the oxygen-air ratio is (n-x) to (x-0.21) is obtained by the oxygen enrichment ratio x percent and the proportion y percent of the conventional air in the oxygen-enriched air;
the combustion control system sets the pressure and the opening of the flow regulating valve through the numerical calculation and the actual heat load of the furnace to regulate the actually supplied oxygen amount, and the metering, the indicating and the recording are carried out through an oxygen pipeline flowmeter; the amount of the conventional air supplied by the oxygen-enriched combustion system is regulated by an inlet regulating valve of a blower, and metering, indicating and recording are carried out by an air main pipe flow meter; meanwhile, a hot air pipeline is arranged on the hot air pipeline behind the oxygen mixing point, and oxygen analysis is carried out on the mixed actual oxygen-enriched concentration so as to dynamically correct the oxygen-air ratio value.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN202111131032.1A CN113790607A (en) | 2021-09-26 | 2021-09-26 | Oxygen-enriched combustion system for steel rolling heating furnace and heat treatment furnace and control method |
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| CN202111131032.1A CN113790607A (en) | 2021-09-26 | 2021-09-26 | Oxygen-enriched combustion system for steel rolling heating furnace and heat treatment furnace and control method |
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| CN202111131032.1A Pending CN113790607A (en) | 2021-09-26 | 2021-09-26 | Oxygen-enriched combustion system for steel rolling heating furnace and heat treatment furnace and control method |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN115354140A (en) * | 2022-08-18 | 2022-11-18 | 重庆赛迪热工环保工程技术有限公司 | Oxygen-enriched heating furnace system and control process |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115354140A (en) * | 2022-08-18 | 2022-11-18 | 重庆赛迪热工环保工程技术有限公司 | Oxygen-enriched heating furnace system and control process |
| CN115354140B (en) * | 2022-08-18 | 2023-08-15 | 重庆赛迪热工环保工程技术有限公司 | Oxygen-enriched heating furnace system |
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