CN102221111A - Temperature control pressure valve and temperature control pressure valve for coke oven - Google Patents
Temperature control pressure valve and temperature control pressure valve for coke oven Download PDFInfo
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- CN102221111A CN102221111A CN2011100746653A CN201110074665A CN102221111A CN 102221111 A CN102221111 A CN 102221111A CN 2011100746653 A CN2011100746653 A CN 2011100746653A CN 201110074665 A CN201110074665 A CN 201110074665A CN 102221111 A CN102221111 A CN 102221111A
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Abstract
The invention relates to an automatic control device, in particular to an automatic control device for realizing pressure control through temperature and application thereof in a coke oven. Aiming at a plurality of problems in the pressure detecting control valve at present, the invention provides a temperature control pressure valve, comprising a temperature sensor, a controller and an acting device, wherein the temperature sensor is used for acquiring temperature signals and transferring the temperature signals to the controller; a control module in the controller is used for analyzing the temperature signals, converting the temperature signals into command signals and transferring the command signals to the acting device; and the acting device is used for driving an air flow regulating device to operate. According to the temperature control p0ressure valve, the human resource is saved; the control accuracy is improved; the detecting error caused by graphite caked on the pressure detecting surface is avoided; and the temperature change and the pressure in a carbonization chamber are contacted to adapt to the dust environment; thus the detecting precision is higher; and the pressure control demands are satisfied.
Description
Technical field
The present invention relates to a kind of automatic controller, especially relate to by temperature and realize pressure controlled automatic controller and the application in coke oven thereof.
Background technique
At present, control for liquid flux generally all is the method that adopts pressure control valve, that is to say, by the pressure in the monitoring confined space, the control valve aperture, and then keep the pressure stability of confined space, bigger for variation in pressure, pressure detecting system is difficult for installing, the detection of installation back is affected by environment easily, use the susceptible situation of accuracy for a long time, uses by the technology of Pressure testing and then control valve aperture just to be restricted.
A kind of situation that the coking production technology comes to this.The testing coke oven of conventional coke making process is the intermittent type chamber type coke furnace.In the coking production process, the discharge capacity of raw coke oven gas changes along with the difference of process of coking, and at the coking initial stage, the discharge capacity of raw coke oven gas is big, and the pressure in the coke oven is big, and is not smooth if raw coke oven gas is dredged, and can cause furnace roof, fire door to run cigarette and burn with anger befouling environment; In the mid-term of coking, the volatile substance in the coal charge is discharged gradually, and the discharge capacity of raw coke oven gas reduces gradually; In the latter stage of coking, the raw coke oven gas major part is the gas of Pintsch process, and the coal gas amount is very little, need in time close the asending pipe valve, keep the slight positive pressure state in the coke oven, otherwise can make air enter coke oven, burn the coke in the coke oven, influence production testing.
Exist than big-difference because each time period of coking process produces the coal gas amount, keep stable for making the coke oven production testing, its key issue is and must carries out real-time regulated to carbonization chamber pressure.
For avoiding carbonization chamber negative pressure to occur, normal by the artificial method of adjusting at any time of observing at any time, according to the pressure gauge that detects asending pipe, the asending pipe valve opening is put in order in messenger's wage adjustment, but not only waste time and energy by manual tune, and precision and the amplitude adjusted are difficult to effective control.
Patent " medium-sized electric heating testing coke oven " has adopted the automatic pressure detection system, adjust the aperture of asending pipe valve according to automatic detected pressure value, solved self-adjusting problem like this, but pressure detecting system is worked under the bigger raw coke oven gas environment of dust loading for a long time, usually cause and detect a mouthful calculus China ink, detect a mouthful obstruction, thereby have influence on the precision of detection, therefore the accuracy of adjusting the asending pipe valve according to automatic detected pressure also is affected, pressure that can not better controlled coke oven carbonization chamber.
Summary of the invention
Various problems at present Pressure testing control valve existence, the inventor provides a kind of temperaturing control pressure valve, comprise temperature transducer, controller, executor, described temperature transducer collecting temperature signal, and temperature signal is passed to controller, the control module in the controller is to the temperature signal analysing and processing, and is converted into command signal, be passed to executor, executor drives the gas flow adjusting means running.Thereby the control of pressure valve is converted into temperature detection by Pressure testing, because the Fluid Volume difference, its temperature certainly exists difference, and the size that how much has determined hydrodynamic pressure of Fluid Volume, so the direct size of reacting fluid pressure of fluid temperature (F.T.).In view of the above, at first the pressure criteria in the enclosed space is converted into temperature standard, and this temperature standard is preset in the middle of the control module of controller, after receiving the temperature signal that the temperature transducer collection transmits, by with preset temperature comparison, and then the signal of giving an order, be passed to executor, and have executor to drive the controlling device running, and then the fluid flow amount of control confined space, keep the stable of confined space pressure.
As the application of this temperaturing control pressure valve in coke oven, the inventor has done further adaptation, comprise temperature transducer, controller, executor, described temperature transducer links to each other with the asending pipe of coke furnace carbonization chamber, described executor links to each other with the asending pipe valve of coke furnace carbonization chamber, temperature signal in the described temperature transducer online acquisition asending pipe, and temperature signal is passed to controller, control module in the controller is to the temperature signal analysing and processing, and be converted into command signal, and being passed to executor, executor drives the asending pipe valve event.At the coking initial stage, the discharge capacity of raw coke oven gas is big, and the pressure in the coke oven is big, temperature is high, and the control module in the controller requires executor to drive the increase of asending pipe valve opening, thereby increases Throughput, avoids furnace roof, fire door to run cigarette and burns with anger befouling environment; In the mid-term of coking, the volatile substance in the coal charge is discharged gradually, and the discharge capacity of raw coke oven gas reduces gradually, thereby its temperature reduces, and the control module in the controller is by the analysing and processing to temperature, and the command action device drives the asending pipe valve opening and reduces; In the latter stage of coking, the raw coke oven gas major part is the gas of Pintsch process, the coal gas amount is very little, temperature is very low, controller is after to this low temperature analysing and processing, send the order of closing the asending pipe valve, thereby keep the slight positive pressure state in the coke oven, avoid air to enter coke oven, burn the coke in the coke oven, influence production testing.Thereby real-time, the adjusting automatically of asending pipe pressure have been realized.
In sum, it is conspicuous adopting the beneficial effect that the present invention produced, and at first, adopts the automatic controller of asending pipe valve, has replaced manual control, has saved human resources, has improved the accuracy of control; Secondly, adopt temperature control to replace traditional pressure control, avoided the detection error that causes because of Pressure testing surface calculus China ink; At last, temperature variation and carbonization chamber internal pressure are connected, and the environment of temperature detection adaptation dust, testing precision is higher, has satisfied pressure controlled requirement.
Description of drawings
Fig. 1 asending pipe valve automatic controller schematic representation
Fig. 2 asending pipe valve automatic controller side view
Wherein 1-temperature transducer, 2-increase in pipeline, 3-asending pipe valve, 4-executor, 5-controller, 6-carbonization chamber.
Embodiment
As depicted in figs. 1 and 2, the raw coke oven gas that coking produces is generated in process of coking by carbonization chamber 6, by increase in pipeline 2, temperature data in the temperature transducer 1 online acquisition increase in pipeline 2 and with data transmission to controller 5, control module in the controller 5 is handled, is analyzed temperature data, and executor 4 is sent action command, and executor 4 drives 3 motions of asending pipe valve, and the aperture by asending pipe valve 3 changes gas flow area, and then guarantees the pressure stability in the carbonization chamber 6.Specifically, at the coking initial stage, the discharge capacity of raw coke oven gas is big, the gas of increase in pipeline 2 of flowing through is many, temperature transducer 1 detected temperature height, and the control module in the controller 5 is handled high-temperature analysis, command action device 4 drives asending pipe valve 3 apertures and increases, thereby the increase Throughput is avoided furnace roof, fire door to run cigarette and is burned with anger befouling environment; In the mid-term of coking, volatile substance in the coal charge is discharged gradually, the discharge capacity of raw coke oven gas reduces gradually, the gas of increase in pipeline 2 of flowing through reduces, temperature transducer 1 detected temperature reduces, control module in the controller 5 is by the analysing and processing to temperature, and command action device 4 drives asending pipe valve 3 apertures and reduces; In the latter stage of coking, the raw coke oven gas major part is the gas of Pintsch process, the coal gas amount is very little, temperature transducer 1 detected temperature is very low, controller 5 is after to this low temperature analysing and processing, send the order of closing asending pipe valve 3, thereby keep the slight positive pressure state in the coke oven, avoid air to enter coke oven, burn the coke in the coke oven, influence production testing.Thereby real-time, the adjusting automatically of asending pipe pressure have been realized.
Claims (2)
1. temperaturing control pressure valve, it is characterized in that: comprise temperature transducer, controller, executor, described temperature transducer collecting temperature signal, and temperature signal is passed to controller, control module in the controller is to the temperature signal analysing and processing, and be converted into command signal, and being passed to executor, executor drives the gas flow adjusting means running.
2. temperaturing control pressure valve that is applicable to coke oven, it is characterized in that: comprise temperature transducer, controller, executor, described temperature transducer links to each other with the asending pipe of coke furnace carbonization chamber, described executor links to each other with the asending pipe valve of coke furnace carbonization chamber, temperature signal in the described temperature transducer online acquisition asending pipe, and temperature signal is passed to controller, control module in the controller is to the temperature signal analysing and processing, and be converted into command signal, be passed to executor, executor drives the asending pipe valve event.
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CN2011100746653A CN102221111A (en) | 2011-03-28 | 2011-03-28 | Temperature control pressure valve and temperature control pressure valve for coke oven |
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CN2011100746653A CN102221111A (en) | 2011-03-28 | 2011-03-28 | Temperature control pressure valve and temperature control pressure valve for coke oven |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105238424A (en) * | 2015-11-20 | 2016-01-13 | 昆明电研新能源科技开发有限公司 | Recognition device for biomass destructive distillation carbonization process |
CN106118696A (en) * | 2016-07-11 | 2016-11-16 | 神木县三江煤化工有限责任公司 | A kind of device and method controlling gas retort air inlet |
CN106774515A (en) * | 2017-01-13 | 2017-05-31 | 山东师范大学 | A kind of heatingup of coke oven battery intelligent temperature control system and control method |
CN109018752A (en) * | 2018-07-05 | 2018-12-18 | 燕山大学 | A kind of gas shield device of serials control |
CN110005843A (en) * | 2019-04-24 | 2019-07-12 | 杭州初始服饰有限公司 | A kind of circulation air guide valve |
CN114526339A (en) * | 2022-04-22 | 2022-05-24 | 陕西祥瑞电气工程自动化有限公司 | Gas flow fine adjuster |
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US3810578A (en) * | 1972-10-17 | 1974-05-14 | Johnson Service Co | Bulb modulating gas valve |
JP2005089507A (en) * | 2003-09-12 | 2005-04-07 | Aisin Seiki Co Ltd | Apparatus for carbonization treatment and method for determining completion of carbonization |
CN101070925A (en) * | 2007-06-04 | 2007-11-14 | 潘兆铿 | Mixed-regulation constant-temperature water valve |
CN101074734A (en) * | 2007-06-20 | 2007-11-21 | 吴爱国 | Electric flow self-balancing adjusting valve and method |
CN101089437A (en) * | 2007-07-31 | 2007-12-19 | 北京同方洁净技术有限公司 | Condensation pressure regulating water-saving valve of automatic regulating preset value |
CN201161994Y (en) * | 2008-01-18 | 2008-12-10 | 上海梅山钢铁股份有限公司 | Medium-sized automatic control electrical heating experiment coke oven |
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2011
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Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
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US3810578A (en) * | 1972-10-17 | 1974-05-14 | Johnson Service Co | Bulb modulating gas valve |
JP2005089507A (en) * | 2003-09-12 | 2005-04-07 | Aisin Seiki Co Ltd | Apparatus for carbonization treatment and method for determining completion of carbonization |
CN101070925A (en) * | 2007-06-04 | 2007-11-14 | 潘兆铿 | Mixed-regulation constant-temperature water valve |
CN101074734A (en) * | 2007-06-20 | 2007-11-21 | 吴爱国 | Electric flow self-balancing adjusting valve and method |
CN101089437A (en) * | 2007-07-31 | 2007-12-19 | 北京同方洁净技术有限公司 | Condensation pressure regulating water-saving valve of automatic regulating preset value |
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105238424A (en) * | 2015-11-20 | 2016-01-13 | 昆明电研新能源科技开发有限公司 | Recognition device for biomass destructive distillation carbonization process |
CN105238424B (en) * | 2015-11-20 | 2018-06-05 | 昆明电研新能源科技开发有限公司 | Biomass carbonization carbonizes the identification device of process |
CN106118696A (en) * | 2016-07-11 | 2016-11-16 | 神木县三江煤化工有限责任公司 | A kind of device and method controlling gas retort air inlet |
CN106774515A (en) * | 2017-01-13 | 2017-05-31 | 山东师范大学 | A kind of heatingup of coke oven battery intelligent temperature control system and control method |
CN109018752A (en) * | 2018-07-05 | 2018-12-18 | 燕山大学 | A kind of gas shield device of serials control |
CN110005843A (en) * | 2019-04-24 | 2019-07-12 | 杭州初始服饰有限公司 | A kind of circulation air guide valve |
CN114526339A (en) * | 2022-04-22 | 2022-05-24 | 陕西祥瑞电气工程自动化有限公司 | Gas flow fine adjuster |
CN114526339B (en) * | 2022-04-22 | 2022-08-09 | 陕西祥瑞电气工程自动化有限公司 | Gas flow fine adjuster |
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Application publication date: 20111019 |