CN203656971U - Residual oxygen analytic combustion control device of hot blast stove - Google Patents
Residual oxygen analytic combustion control device of hot blast stove Download PDFInfo
- Publication number
- CN203656971U CN203656971U CN201420023937.6U CN201420023937U CN203656971U CN 203656971 U CN203656971 U CN 203656971U CN 201420023937 U CN201420023937 U CN 201420023937U CN 203656971 U CN203656971 U CN 203656971U
- Authority
- CN
- China
- Prior art keywords
- hot blast
- blast stove
- combustion
- residual oxygen
- 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.)
- Expired - Lifetime
Links
Images
Landscapes
- Regulation And Control Of Combustion (AREA)
Abstract
Description
技术领域 technical field
本实用新型涉及一种高炉热风炉的燃烧控制装置,属于高炉热风炉燃烧控制设备技术领域。 The utility model relates to a combustion control device for a blast furnace hot blast stove, which belongs to the technical field of blast furnace hot blast stove combustion control equipment.
背景技术 Background technique
在高炉热风炉的运行过程中,需要通过燃烧控制装置对热风炉的燃烧进行有效控制,目前,确定热风炉燃烧控制装置的初始空燃比的主要方法是依靠大量的历史数据,根据历史拱顶温度与空燃比的对应关系确定空燃比的值;另一种方法是根据以往燃烧经验值确定本次燃烧过程初始空燃比的值。这两种方法都会由于热风炉工况的复杂性和和经验误差而不能实现对热风炉燃烧的实时和精确地控制,造成安全可靠性差、煤气消耗高、减排效果差等问题。 During the operation of blast furnace hot blast stove, it is necessary to effectively control the combustion of the hot blast stove through the combustion control device. At present, the main method to determine the initial air-fuel ratio of the hot blast stove combustion control device is to rely on a large amount of historical data. According to the historical vault temperature The corresponding relationship with the air-fuel ratio determines the value of the air-fuel ratio; another method is to determine the value of the initial air-fuel ratio of the combustion process according to the past combustion experience. These two methods will not be able to realize real-time and precise control of the hot blast stove combustion due to the complexity of the hot blast stove working conditions and empirical errors, resulting in problems such as poor safety and reliability, high gas consumption, and poor emission reduction effects.
实用新型内容 Utility model content
本实用新型所要解决的技术问题是提供一种热风炉残氧分析燃烧控制装置,这种装置是将残氧分析与热风炉燃烧控制集成为一体,提供热风炉在快速燃烧期的最佳空燃比,并为下一期燃烧过程提供最佳空燃比基数,同时在热风炉燃烧管理期起到调整空燃比的作用,实现煤气充分燃烧,最大限度地节约热风炉煤气使用量,降低燃烧成本,减少环境污染。 The technical problem to be solved by the utility model is to provide a residual oxygen analysis and combustion control device for the hot blast stove, which integrates the residual oxygen analysis and the combustion control of the hot blast stove, and provides the best air-fuel ratio for the hot blast stove during the rapid combustion period , and provide the best air-fuel ratio base for the next combustion process, and at the same time play a role in adjusting the air-fuel ratio in the combustion management period of the hot blast stove, realize the full combustion of gas, save the gas consumption of the hot blast stove to the greatest extent, reduce combustion costs, and reduce environmental pollution.
解决上述技术问题的技术方案是: The technical scheme that solves the above-mentioned technical problem is:
一种热风炉残氧分析燃烧控制装置,它的构成中包括燃烧控制器、隔离器、废气热电偶、拱顶热电偶、煤气调节阀、空气调节阀、煤气流量计、空气流量计,废气热电偶、拱顶热电偶、煤气流量计、空气流量计分别安装在热风炉上,它们的信号输出端通过隔离器与燃烧控制器的信号输入端相连接,它还增加了残氧分析仪,残氧分析仪安装在热风炉的烟气管道上,残氧分析仪的信号输出端与燃烧控制器的信号输入端相连接。 A combustion control device for residual oxygen analysis of a hot blast stove, which consists of a combustion controller, an isolator, an exhaust gas thermocouple, a vault thermocouple, a gas regulating valve, an air regulating valve, a gas flow meter, an air flow meter, an exhaust gas thermoelectric Couple, vault thermocouple, gas flowmeter, and air flowmeter are respectively installed on the hot blast stove, and their signal output terminals are connected to the signal input terminal of the combustion controller through an isolator. The oxygen analyzer is installed on the flue gas pipe of the hot blast stove, and the signal output end of the residual oxygen analyzer is connected with the signal input end of the combustion controller.
上述热风炉残氧分析燃烧控制装置,所述燃烧控制器的信号输出端与热风炉的煤气输入管道上的煤气调节阀、空气输入管道上的空气调节阀相连接。 In the combustion control device for residual oxygen analysis of the hot blast stove, the signal output end of the combustion controller is connected to the gas regulating valve on the gas input pipeline of the hot blast stove and the air regulating valve on the air input pipeline.
本实用新型的有益效果是: The beneficial effects of the utility model are:
本实用新型是将残氧分析与热风炉燃烧控制高度集成的一体化控制器,以烟气中含氧量的大小作为控制燃烧效率的指标,初步将氧含量回路控制器的设定值设定在平均值0.2%,将残氧分析仪所测得的含氧量作为回路控制器的反馈值。空燃比在每个热风炉烧炉前设定一个基准点,围绕这个基准点,根据氧量回路控制器输出的大小对空燃比基准点进行修正,结果作为参与控制空燃比的设定值,使空燃比即迅速准确又安全地调节至最佳值,使空气与煤气充分燃烧,减少了煤气的使用,降低了空气的污染,在节能方面取得较好的经济效益,节能量在5%以上。 The utility model is an integrated controller which highly integrates the analysis of residual oxygen and the combustion control of the hot blast stove. The oxygen content in the flue gas is used as an index to control the combustion efficiency, and the setting value of the oxygen content loop controller is preliminarily set. At the average value of 0.2%, the oxygen content measured by the residual oxygen analyzer is used as the feedback value of the loop controller. The air-fuel ratio sets a reference point before each hot blast stove is fired. Around this reference point, the air-fuel ratio reference point is corrected according to the output of the oxygen loop controller. The result is used as the set value for participating in the control of the air-fuel ratio. The air-fuel ratio can be quickly, accurately and safely adjusted to the optimal value, so that the air and gas can be fully combusted, reducing the use of gas and air pollution, and achieving good economic benefits in terms of energy saving, with energy saving of more than 5%.
附图说明 Description of drawings
图1是本实用新型的结构方框图; Fig. 1 is a structural block diagram of the utility model;
图2是本实用新型的结构示意图。 Fig. 2 is a schematic structural view of the utility model.
图中标记如下:残氧分析仪1、废气热电偶2、拱顶热电偶3、煤气调节阀4、空气调节阀5、煤气流量计6、空气流量计7、燃烧控制器8、可编程序控制器9、隔离器10、热风炉11。
The marks in the figure are as follows: residual oxygen analyzer 1,
具体实施方式 Detailed ways
本实用新型的构成中包括残氧分析仪1、废气热电偶2、拱顶热电偶3、煤气调节阀4、空气调节阀5、煤气流量计6、空气流量计7、燃烧控制器8、隔离器10。
The composition of the utility model includes a residual oxygen analyzer 1, an
图中显示,废气热电偶2、拱顶热电偶3、煤气流量计6、空气流量计7分别安装热风炉11上,它们的信号输出端通过隔离器10与燃烧控制器8的信号输入端相连接。
As shown in the figure, the
废气热电偶2的作用是测量废气温度,拱顶热电偶3用于测量拱顶温度,煤气调节阀4用于控制煤气流量,空气调节阀5用于控制空气流量,煤气流量计6用于测量煤气流量,空气流量计7用于测量空气流量,燃烧控制器8的作用是根据反馈的拱顶温度、废气温度、残氧量等数据调节煤气调节阀4和空气调节阀5,隔离器10用于分流信号。
The function of the
图中显示,残氧分析仪1安装在热风炉11的烟气管道上,残氧分析仪1的信号输出端与燃烧控制器8的信号输入端相连接。残氧分析仪的作用是测量烟气中的含氧量。
As shown in the figure, the residual oxygen analyzer 1 is installed on the flue gas pipeline of the
图中显示,废气热电偶2、拱顶热电偶3、煤气流量计6、空气流量计7通过隔离器10将信号一分为二分别连接至可编程序控制器9和燃烧控制器8,同时残氧分析仪1将废气残氧信号传至燃烧控制器8,且可编程序控制器9与燃烧控制器8做通讯,燃烧控制器8根据现场反馈的数调节煤气调节阀4和空气调节阀5。
As shown in the figure, the
本实用新型的工作过程如下: The working process of the present utility model is as follows:
手动切换至“自动烧炉”,点击“开始烧炉”,热风炉11的煤气调节阀4、空气调节阀5开始缓慢打开,煤气调节阀4打开至初始煤气量时停止,空气调节阀5根据初始空燃比调节,进入快速燃烧期,残氧分析仪1开始测量烟气中的氧含量,根据理论计算,含氧量控制器设定值一般设定在0.2%有,但有一定的纹波,只要波动在0.0%~0.3%即可。在控制器死区设计上,在0.1%~0.2%区间控制器输出不作变化,特别是含氧量小于0.1%持续时间小于5s的认为是好的,控制器无须动作。如果持续小于0.1%5s以上并等于0.0%2s以上,控制器需动作,加大空气阀门,使含氧量控制到0.1%以上,同理可用在含氧量大于0.2%的判断上。控制系统会记忆氧含量在在0.1%~0.2%区间的空燃比,作为下次燃烧的基准数据,之后燃烧系统进入拱顶管理区及废气管理区,直到燃烧结束。
Manually switch to "Auto Burning Furnace", click "Start Furnace Burning", the gas regulating valve 4 and
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420023937.6U CN203656971U (en) | 2014-01-15 | 2014-01-15 | Residual oxygen analytic combustion control device of hot blast stove |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420023937.6U CN203656971U (en) | 2014-01-15 | 2014-01-15 | Residual oxygen analytic combustion control device of hot blast stove |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203656971U true CN203656971U (en) | 2014-06-18 |
Family
ID=50923351
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420023937.6U Expired - Lifetime CN203656971U (en) | 2014-01-15 | 2014-01-15 | Residual oxygen analytic combustion control device of hot blast stove |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203656971U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104534504A (en) * | 2014-12-25 | 2015-04-22 | 河北钢铁股份有限公司承德分公司 | Rotary kiln combustion control device and method |
| CN106352339A (en) * | 2016-11-01 | 2017-01-25 | 深圳德尔科机电环保科技有限公司 | Optimal control system for air-fuel ratio of gas heating furnace |
| CN108458486A (en) * | 2018-04-13 | 2018-08-28 | 安徽工业大学 | A kind of Combustion of Hot Air Furnace automatic control system and its control method |
| CN114350877A (en) * | 2022-01-10 | 2022-04-15 | 广东韶钢松山股份有限公司 | Hot-blast stove baking method |
-
2014
- 2014-01-15 CN CN201420023937.6U patent/CN203656971U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104534504A (en) * | 2014-12-25 | 2015-04-22 | 河北钢铁股份有限公司承德分公司 | Rotary kiln combustion control device and method |
| CN104534504B (en) * | 2014-12-25 | 2017-01-18 | 河北钢铁股份有限公司承德分公司 | Rotary kiln combustion control device and method |
| CN106352339A (en) * | 2016-11-01 | 2017-01-25 | 深圳德尔科机电环保科技有限公司 | Optimal control system for air-fuel ratio of gas heating furnace |
| CN106352339B (en) * | 2016-11-01 | 2018-06-08 | 深圳德尔科机电环保科技有限公司 | A kind of gas-fired heater optimization of air-fuel ratio control system |
| CN108458486A (en) * | 2018-04-13 | 2018-08-28 | 安徽工业大学 | A kind of Combustion of Hot Air Furnace automatic control system and its control method |
| CN114350877A (en) * | 2022-01-10 | 2022-04-15 | 广东韶钢松山股份有限公司 | Hot-blast stove baking method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105387458B (en) | It is a kind of to reduce the system and method for combustion apparatus discharged nitrous oxides | |
| CN101892338B (en) | Constant wind temperature control system for hot blast stove | |
| CN103486607B (en) | Automatic fuel adjustment system and method of multi-fuel fired boiler | |
| CN103305683B (en) | A control system and method for burner combustion of continuous annealing furnace under low power | |
| CN203656971U (en) | Residual oxygen analytic combustion control device of hot blast stove | |
| CN204536959U (en) | A kind of FGD device Predictive Control System for coal-burning power plant | |
| CN205191552U (en) | System for it discharges to reduce combustion apparatus nitrogen oxide | |
| CN110566962A (en) | Combustion control method of heat accumulating type single-burner aluminum melting furnace with adjustable air-fuel ratio | |
| CN103090683B (en) | Method for controlling furnace pressure of pulse furnace | |
| CN109579044A (en) | Air-fuel ratio dynamic feedforward combustion control method for walking beam furnace | |
| CN203298342U (en) | Combustion control system of heat treatment furnace | |
| CN202521629U (en) | Natural gas three-level pressure regulating device of shuttle kiln | |
| CN207584816U (en) | The coefficient of excess air management system of kiln | |
| CN108949193A (en) | Coke oven exhaust gas circulation automatic control system and method | |
| CN100454182C (en) | High manganese steel frog heat treatment system and heat treatment process | |
| CN207600230U (en) | Sintering ignition furnace fuel control system | |
| CN103073203B (en) | Sleeve kiln energy consumption monitoring system and control method thereof | |
| CN203240767U (en) | Hot blast stove combustion optimal control system | |
| CN110713851A (en) | Automatic adjusting method for mixed heat value of three gases of blast furnace coke oven converter | |
| CN102338695B (en) | The calibration system of direct-combustion burner of industrial furnace and method | |
| CN105648130A (en) | Automatic ignition control system and method for stove burning of hot blast stove | |
| CN204693481U (en) | A kind of many burner combustions energy-conserving regulate and control system | |
| CN201762280U (en) | Coal gas regulating device used for heating coke oven | |
| CN205535931U (en) | A gas control system for tea processing | |
| CN110220312B (en) | Control method for gas water heater and gas water heater |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 2316-04, Block B, Binjiang Business Building, No. 158, Zhongshan East Road, Qiaoxi District, Shijiazhuang City, Hebei Province, 050000 Patentee after: Hebei Hanyao Carbon New Energy Technology Co.,Ltd. Address before: Room 2315, Block B, Binjiang Business Building, No. 158, Zhongshan East Road, Shijiazhuang City, Hebei Province, 050000 Patentee before: HEBEI HANYAO ENVIRONMENTAL PROTECTION TECHNOLOGY CO.,LTD. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140618 |