WO2014101785A1 - Method and system for controlling air quantity of air box of sintering trolley - Google Patents
Method and system for controlling air quantity of air box of sintering trolley Download PDFInfo
- Publication number
- WO2014101785A1 WO2014101785A1 PCT/CN2013/090513 CN2013090513W WO2014101785A1 WO 2014101785 A1 WO2014101785 A1 WO 2014101785A1 CN 2013090513 W CN2013090513 W CN 2013090513W WO 2014101785 A1 WO2014101785 A1 WO 2014101785A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- air
- air volume
- large flue
- valve
- valve opening
- Prior art date
Links
- 238000005245 sintering Methods 0.000 title claims abstract description 138
- 238000000034 method Methods 0.000 title claims abstract description 65
- 238000005070 sampling Methods 0.000 claims description 40
- 230000008569 process Effects 0.000 claims description 26
- 239000000779 smoke Substances 0.000 claims description 6
- 230000003247 decreasing effect Effects 0.000 abstract description 5
- 239000002699 waste material Substances 0.000 abstract description 5
- 239000000463 material Substances 0.000 description 14
- 230000001276 controlling effect Effects 0.000 description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical group [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 7
- 229910052742 iron Inorganic materials 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000003546 flue gas Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 1
- 241001062472 Stokellia anisodon Species 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000009770 conventional sintering Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001595 flow curve Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000009865 steel metallurgy Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B21/00—Open or uncovered sintering apparatus; Other heat-treatment apparatus of like construction
- F27B21/06—Endless-strand sintering machines
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B21/00—Open or uncovered sintering apparatus; Other heat-treatment apparatus of like construction
- F27B21/04—Sintering pots or sintering pans
Definitions
- the invention relates to an energy-saving technology of a sintering system in the metallurgical field, and in particular to a method and a system for controlling the air volume of a sintering trolley. Background technique
- the sintering system mainly includes a plurality of equipments such as a sintering trolley, a mixer, a main exhauster, a ring cooler, etc.
- the overall process flow is shown in Fig. 1: Various raw materials are proportioned in the batching chamber 1, and then enter the mixer 2 The mixing hook and the plucking are carried out, and then the materials are hooked on the sintering trolley 5 by the round roller feeder 3 and the nine-roller distributing machine 4, and the ignition fan 6 and the igniting fan 7 are ignited by the material, and the obtained after the sintering is completed.
- the sintered ore is crushed by the single-roll crusher 8 and then enters the ring-cooling machine 9 for cooling, and finally sieved and granulated and sent to the blast furnace or the finished mineral warehouse.
- the oxygen required for the sintering reaction is provided by the main exhaust fan 10.
- the material runs forward with the sintering carriage 5, and the position of the material on the sintering trolley 5 when sintering is completed is referred to as the sintering end point. It is necessary to ensure that the sintering end point does not deviate during sintering. If the sintering end point deviates due to various reasons, the traditional method is to adjust the speed of the sintering trolley to Yes: If the sintering end point is ahead, the running speed of the trolley will be accelerated; on the contrary, if the sintering end point is behind, the running speed of the trolley will be slowed down.
- the above is the basic situation of the sintering process and the sintering system.
- the main exhaust fan 10 is a large power consumer, and in the conventional sintering process, the main exhaust fan 10 will always operate at full load, thereby causing a great waste of energy.
- One energy saving scheme in the prior art is: predicting the sintering end point by detecting the flue gas temperature of each bellows, and maximizing the yield by adjusting the speed of the sintering trolley to ensure the quality of the sintering, in the scheme
- the control of the air volume is mainly achieved by controlling the valve between the main exhaust fan and the flue, and basically also the manual adjustment process.
- the object of the embodiments of the present invention is to provide a method and system for controlling the air volume of a sintering trolley bellows, and to improve the energy saving effect of the main exhaust fan by adjusting the air volume of each bellows.
- an embodiment of the present invention provides a method for controlling a wind volume of a sintering trolley, wherein each of the bellows of the sintering trolley is provided with a valve, and the method includes:
- the valve opening of the other bellows is adjusted according to the air volume of the specified bellows and the relationship between the air volume of each bellows in the database and the valve opening degree of the corresponding valve, so that the air volume of the other bellows is consistent with the air volume of the designated bellows.
- the method further includes:
- the method further includes:
- the method further comprises:
- the valve opening of the first designated bellows group is adjusted to return the sintering end point to normal, wherein the first designated bellows group includes a plurality of bellows.
- the method further comprises:
- the current large flue air volume and the current large flue effective wind rate are sampled multiple times, and the current large flue air volume and the large flue air volume preset value, the current large flue effective wind rate and the large smoke are judged after each sampling.
- the valve in the second designated bellows group is opened in each sampling period. The degree is reduced by 2%.
- the valve opening degree in the third designated bellows group is reduced by 2% in each sampling period until the current large smoke
- the amount of road air reaches the preset value of the large flue air volume and the current effective flue rate of the large flue reaches the preset value of the effective flue rate of the large flue;
- the valve in the third designated bellows group is opened in each sampling period. The degree is increased by 2%.
- the valve opening degree in the third designated bellows group reaches 100%
- the valve opening degree in the second designated bellows group is increased by 2% in each sampling period until the current large flue air volume reaches The preset value of the large flue air volume and the current effective flue rate of the large flue reaches the preset value of the effective flue rate of the large flue;
- the bellows in the third designated bellows group are located before the second designated bellows group.
- the method further comprises:
- valve opening of the bellows is reduced while the other bellows valve opening is increased.
- an embodiment of the present invention further provides a sintering trolley air box air volume control system, wherein each of the bellows of the sintering trolley is provided with a valve, and the system includes:
- An air volume collecting unit configured to collect air volume of the specified bellows of the sintering trolley
- the first valve adjusting unit adjusts the valve opening degree of the other bellows according to the air volume of the specified bellows and the relationship between the air volume of each bellows in the database and the valve opening degree of the corresponding valve, so that the air volume of the other bellows and the designated bellows The air volume is consistent.
- the system further includes:
- the database initializing unit is configured to: for each valve, collect air volume data of the bellows where the valve is located during the valve opening and closing process, and obtain a relationship between the valve opening degree and the air volume and record in the database.
- the system further includes:
- the database updating unit is configured to: for each valve, re-acquire the air volume data of the bellows where the valve is located during the valve opening and closing process, obtain a new relationship between the valve opening degree and the air volume, and update the database.
- the system further includes:
- a sintering end point judging unit for judging whether an end point of the sintering is shifted
- a second valve adjusting unit configured to adjust a valve opening degree of the first designated bellows group to return to a normal state when the end point of the sintering is shifted, wherein the first designated bellows group includes a plurality of bellows.
- the system further includes:
- the sampling and judging unit is configured to perform multiple sampling on the current large flue air volume and the current large flue effective wind rate, and determine the current large flue air volume and the large flue air volume preset value and the current large smoke after each sampling.
- the third valve adjusting unit is configured to: if the current large flue air volume is greater than the preset value of the large flue air volume and the current large flue effective wind rate is less than the preset value of the large flue effective wind rate, then each sampling period will be The valve opening degree in the second designated bellows group is reduced by 2%, and when the valve opening degree in the second designated bellows group is decreased by 8%, the valve opening degree in the third designated bellows group is again in each sampling period.
- the valve opening degree in the third designated bellows group is increased by 2% in each sampling period, when the third designated bellows group is When the valve opening reaches 100%, the valve opening degree in the second designated bellows group is increased by 2% in each sampling period until the current large flue air volume reaches the preset value of the large flue air volume and the current large flue The effective wind rate reaches the preset value of the effective flue rate of the large flue;
- the bellows in the third designated bellows group are located before the second designated bellows group.
- the system further includes:
- the fourth valve regulating unit is used for: When it is necessary to increase the vertical sintering speed at any of the bellows, increase the valve opening of the bellows while reducing the opening of other bellows valves; when it is required to reduce the vertical sintering speed at any of the bellows, reduce the bellows Valve opening, while increasing the opening of other bellows valves.
- the embodiment of the invention collects the air volume data of the designated bellows of the sintering trolley, and adjusts the valve opening degree of the other bellows according to the air volume data of the specified bellows and the relationship between the air volume of each bellows in the database and the opening degree of the corresponding bellows valve, so that each The actual air volume in the bellows is as close as possible to the required air volume, thus avoiding the situation that the proportion of effective wind in the bellows is gradually reduced, greatly reducing the waste of air volume and saving energy more effectively. It also avoids the situation where the vertical sintering speed is constantly increasing, reducing the generation of ineffective air volume and ensuring the quality of the sintered ore.
- the embodiment of the invention can also adjust the valve opening degree of some bellows when the end point of the sintering occurs, which can effectively return the sintering end point to normal, so that not only the sintering end point can be corrected more accurately, but also the adjustment can be achieved.
- the purpose of sintering the speed of the trolley is to keep the speed of the sintering trolley constant, which is convenient for subsequent processing.
- Figure 1 is a schematic view of a typical sintering system
- FIG. 2 is a flow chart of a method according to an embodiment of the present invention.
- Embodiment 3 is a flow chart of a method according to Embodiment 2 of the present invention.
- Figure 5 is a schematic diagram of a system of the fourth embodiment of the present invention. detailed description
- Embodiment 1 is a diagrammatic representation of Embodiment 1:
- the material to be sintered on the sintering trolley consists of multiple layers.
- the wind that participates in the physical and chemical reaction of the material during sintering is called effective wind.
- Other winds that do not participate in the reaction are called ineffective wind.
- the inventors are implementing the invention During the process, it is found that as the sintering progresses, the thickness of each layer of the material will change, and the sinter layer with better gas permeability will continue to thicken, while the thickness of other layers will gradually decrease, that is, the resistance of the layer gradually increases with the sintering process.
- the air volume entering the bellows will gradually increase, resulting in a gradual decrease in the proportion of effective winds, an increase in ineffective winds, and a waste of air volume, and excessive ineffective air volume will not only cause the main The consumption of electric energy will also cause heat loss.
- the gradual increase of the air volume of the bellows will also accelerate the vertical sintering speed, seriously affecting the quality of the sinter. Therefore, in order to better adjust the air volume, ensure that the air volume is not wasted, and effectively save energy, the basic idea of this embodiment is: Add an adjustable valve for each bellows on the sintering trolley, and adjust the opening of some bellows valves.
- the speed of the sintering trolley is controlled during sintering, that is, the speed of the sintering trolley is not constant, and in the present embodiment, the preferred speed of the sintering trolley is constant. In this way, it is simpler to collect the air volume, obtain the relationship between the air volume and the valve opening degree, reduce the complexity of the method, and be easy to implement.
- the speed of the sintering trolley is constant, the sintering yield is also stabilized, which facilitates the handling of subsequent processes. The following description assumes that the speed of the sintering trolley is constant.
- the method is a sintering trolley air volume control method, and each bellows of the sintering trolley is provided with a valve, and the method includes:
- an air volume detecting device can be provided in each of the bellows of the sintering cart.
- the collection may be real-time acquisition, or the windbox air volume information may be collected every other sampling period T.
- the premise of this step is that the current sintering end position is within the normal range, and the vertical sintering speed is also in compliance.
- the air volume of the other bellows is controlled by the air volume of a specified bellows.
- the designated bellows can be selected from the middle of the bellows, for example, the twelfth bellows, that is, from the end of the ignition.
- the twelfth bellows because the vertical sintering speed at the position of the bellows is usually equal to or closest to the specified vertical sintering speed.
- the specific embodiment of the present invention is not limited to the specific location of the specified bellows.
- valve opening degree adjusts the valve opening of the other bellows so that the air volume of the other bellows is consistent with the air volume of the designated bellows.
- the process of acquisition-adjustment in the above steps may be performed every other period T.
- the relationship between the air volume of each bellows and the valve opening degree is preset in the database. After collecting the air volume data of the specified bellows, the database can be used to know how the air opening of the other bellows should be the same as that of the other bellows, so that the valve opening of each of the other bellows should be The valve opening degree adjusts the valve, so that the air volume of other bellows is always consistent with the air volume of the specified bellows, thereby ensuring that the air volume is not wasted, saving energy, and also making the vertical sintering speed effectively controlled.
- the relationship between the amount of airflow in each of the bellows and the valve opening degree in the database can be obtained by various methods, for example, by experiment or experience, and the embodiment of the present invention does not impose any limitation.
- the relationship between the valve opening and the air volume in the database can be obtained by, for example, before step S201,
- the air volume of the bellows where the valve is located is collected, and the relationship between the valve opening degree and the air volume is obtained and recorded in the database.
- the air volume detecting device installed in the wind box can detect the wind volume of the wind box in the production process in real time, and input the air valve opening degree and air volume information in the production process into the industrial computer as a database storage, and can also be fitted into the valve opening degree. Air flow curve with bellows.
- the step of updating the database may be further included, that is, after S202, the method may further include:
- This embodiment is based on the previous embodiment and is a further extension of the previous embodiment.
- the idea is: If the end point of the sintering is found to be offset during the sintering process, the bellows valves can be fine-tuned, and the end point of the sintering is changed by controlling the air volume of the bellows to return the sintering end point to a reasonable position. This not only can correct the sintering end point more accurately, but also achieve the purpose of not adjusting the speed of the sintering trolley, so that the speed of the sintering trolley can be kept constant, which is convenient for the subsequent process.
- FIG. 3 is a flowchart of the method according to the second embodiment of the present invention. After the step S202 of the previous embodiment, the method may further include:
- the total length of the sintering trolley is 90m, and 20 bellows are used. Each bellows is given the number 1 ⁇ 20 according to the distance from the igniter or the nose. The coordinates of the latter bellows can be seen in the table. 1.
- the sintering end position is divided into five levels: front, front, normal, later, and after (the "front” refers to the current sintering end point closer to the end of the head than the ideal sintering end point, "back” exactly the opposite).
- the best position for the sintering end point is the penultimate bellows position, that is, the bellows No. 19.
- the front end is expressed as the end point of sintering before 79m, compared with 79m ⁇ 83m in the front, 85m ⁇ 87m in the later, and 87m later.
- the judgment of the sintering end point is mainly obtained by detecting the temperature of each bellows.
- the position of the material on the trolley is defined as the sintering end point when the material temperature is about 350 degrees. Therefore, the sintering end point control is equivalent to controlling the position of the sintered material within the set position range when the material detection temperature is 350 degrees.
- the specific adjustment strategy for adjusting the valve opening of the first designated bellows group can be as follows:
- the air volume entering the trolley is reduced, the vertical speed of the sintering is reduced, and the valve opening is increased to increase the air volume.
- the valve of the last bellows begins to select a different number of bellows to form the first designated bellows group, as shown in the table below, and the adjustment can be performed with the same amplitude or different amplitude for each relevant valve.
- FIG. 4 is a flow chart of a method according to a third embodiment of the present invention.
- the method is based on the first embodiment and is a further extension based on the first embodiment.
- the following steps may be further performed: S401, the current large flue air volume and the current large flue effective wind The rate is sampled multiple times, and after each sampling, the current relationship between the current large flue air volume and the large flue air volume preset value, the current large flue effective wind rate and the large flue effective wind rate preset value are determined.
- an air volume collecting device can be provided in the large flue to collect the large flue air volume.
- a flue gas analyzer can be installed in the large flue to detect the gas components in the flue gas, and then compared with the gas components of the ordinary air to obtain an effective wind ratio.
- the embodiment of the present invention is not limited.
- the second designated bellows group is selected in each sampling period.
- the valve opening is reduced by 2%.
- the valve opening in the third designated bellows group is reduced by 2% in each sampling period.
- valve opening is reduced by 2% in each sampling period T, when the valve is lowered by 8%, then the front two bellows (15, 16) are adjusted again, each time lowering The opening is still 2% until the control requirements are met.
- the valve opening degree in the third designated bellows group is increased by 2% in each sampling period, and when the valve opening degree in the third designated bellows group reaches 100%, The valve opening degree in the second designated bellows group is increased by 2% in each sampling period until the current large flue air volume reaches the preset value of the large flue air volume and the current large flue effective air rate reaches the large flue effective air rate. default value.
- the 15th and 16th bellows can be selected first, and the valve opening degree is increased by 2% in each sampling period T.
- the valve opening degree is adjusted to 100%, the valve opening degree is fixed, and then the rear two bellows are adjusted (17. 18), the opening is increased by 2% each time until the control requirements are met.
- the bellows in the third designated bellows group are located before the second designated bellows group.
- the second and third designated bellows groups may be determined according to the site conditions, and the embodiments of the present invention are not limited. Embodiment 4
- FIG. 5 is a schematic diagram of a system of the fourth embodiment of the present invention.
- the system is based on the above method embodiment, and is a sintering trolley bellows air volume control system.
- Each of the bellows of the sintering trolley is provided with a valve, and the system includes:
- the air volume collecting unit 501 is configured to collect the air volume of the designated bellows of the sintering trolley;
- the first valve adjusting unit 502 adjusts the valve opening degree of the other bellows according to the air volume of the specified bellows and the relationship between the air volume of each bellows in the database and the valve opening degree of the corresponding valve, so that the air volume of the other bellows and the designation The air volume of the bellows is the same.
- the system further includes:
- the database initializing unit is configured to: for each valve, collect air volume data of the bellows where the valve is located during the valve opening and closing process, obtain a relationship between the valve opening degree and the air volume, and record in the database.
- the system further includes:
- the database updating unit is configured to: for each valve, re-acquire the air volume data of the bellows where the valve is located during the valve opening and closing process, obtain a new relationship between the valve opening degree and the air volume, and update the database.
- the system further includes:
- a sintering end point judging unit for judging whether an end point of the sintering is shifted;
- a second valve adjusting unit configured to adjust a valve opening degree of the first designated windbox group to return to a normal state when the sintering end point is offset, wherein the first designated bellows group includes a plurality of wind boxes.
- the system further includes:
- the sampling and judging unit is configured to perform multiple sampling on the current large flue air volume and the current large flue effective wind rate, and determine the current large flue air volume and the large flue air volume preset value and the current large smoke after each sampling.
- the third valve adjusting unit is configured to: if the current large flue air volume is greater than the preset value of the large flue air volume and the current large flue effective wind rate is less than the preset value of the large flue effective wind rate, then each sampling period will be The valve opening degree in the second designated bellows group is reduced by 2%, and when the valve opening degree in the second designated bellows group is decreased by 8%, the valve opening degree in the third designated bellows group is again in each sampling period.
- the valve opening degree in the third designated bellows group is increased by 2% in each sampling period, when the third designated bellows group is When the valve opening reaches 100%, the valve opening degree in the second designated bellows group is increased by 2% in each sampling period until the current large flue air volume reaches the preset value of the large flue air volume and the current large flue The effective wind rate reaches the preset value of the effective flue rate of the large flue;
- the bellows in the third designated bellows group are located before the second designated bellows group.
- the system further includes:
- the fourth valve regulating unit is used for:
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Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
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BR112015015064-0A BR112015015064B1 (en) | 2012-12-27 | 2013-12-26 | METHOD AND SYSTEM FOR CONTROLING THE AMOUNT OF AIR OF THE SYNTHRIZATION CARTRIDGE BOX. |
RU2015130235A RU2635590C2 (en) | 2012-12-27 | 2013-12-26 | Method and system to control amount of air of agglomeration car air box |
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CN201210579047.9A CN102997671B (en) | 2012-12-27 | 2012-12-27 | Method and system for controlling air volume of air box of sintering trolley |
CN201210579047.9 | 2012-12-27 |
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WO2014101785A1 true WO2014101785A1 (en) | 2014-07-03 |
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BR (1) | BR112015015064B1 (en) |
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CN102997671B (en) * | 2012-12-27 | 2014-12-10 | 中冶长天国际工程有限责任公司 | Method and system for controlling air volume of air box of sintering trolley |
CN103344116B (en) * | 2013-07-05 | 2015-03-25 | 山西太钢不锈钢股份有限公司 | Method of regulating and controlling air volume of sintering machine by using main ventilation valve and rotating speed in combined mode |
CN103363804B (en) * | 2013-07-29 | 2014-11-26 | 中冶长天国际工程有限责任公司 | Method and system for controlling flow of sintering ignition furnace |
CN103744345B (en) * | 2014-01-26 | 2017-02-01 | 深圳市劲拓自动化设备股份有限公司 | Initialization method and system for starting up of sintering furnace controller |
CN106524763B (en) * | 2016-10-28 | 2019-02-19 | 马鞍山钢铁股份有限公司 | A kind of method based on pallet bellows negative pressure reasonable distribution bellows air quantity and the sintering system using it |
CN108398026B (en) * | 2017-02-05 | 2019-06-28 | 鞍钢股份有限公司 | System and method for detecting homogeneity in sintering process |
CN112393300A (en) * | 2020-11-30 | 2021-02-23 | 中船邮轮科技发展有限公司 | Control method and control system for kitchen gas collecting hood |
CN113532136B (en) * | 2021-06-29 | 2022-08-16 | 鞍钢股份有限公司 | Method for reasonably distributing air volume of sintering trolley air box |
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DE1143334B (en) * | 1962-04-03 | 1963-02-07 | Huntington Heberlein And Compa | Method and device for controlling sintering processes |
CN1125839A (en) * | 1994-12-26 | 1996-07-03 | 徐爱民 | Technological method of iron ore sintering for agglumeration |
RU2377322C2 (en) * | 2007-07-23 | 2009-12-27 | Открытое акционерное общество "Северсталь" (ОАО "Северсталь") | Control method of agglomeration process |
CN101441443B (en) * | 2008-09-18 | 2013-10-30 | 中冶长天国际工程有限责任公司 | Data processing method and device of sintering control parameter |
CN101749952B (en) * | 2009-11-13 | 2012-05-16 | 山西太钢不锈钢股份有限公司 | Parameter matching and adjusting method of sintering machine |
CN101963456B (en) * | 2010-11-04 | 2012-06-27 | 中冶长天国际工程有限责任公司 | Control method of thorough-roasting point in roasting process of material and control system |
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JPH05126474A (en) * | 1991-11-06 | 1993-05-21 | Nippon Steel Corp | Method and device for measuring volume of sucked air by sintering machine |
JP2006336026A (en) * | 2005-05-31 | 2006-12-14 | Jfe Steel Kk | Apparatus and method for sintering |
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BR112015015064B1 (en) | 2019-07-09 |
BR112015015064A8 (en) | 2019-06-25 |
CN102997671B (en) | 2014-12-10 |
RU2635590C2 (en) | 2017-11-14 |
RU2015130235A (en) | 2017-02-01 |
CN102997671A (en) | 2013-03-27 |
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