EP0943881B1 - Control process of the conveyance speed in a travelling grate cooler - Google Patents
Control process of the conveyance speed in a travelling grate cooler Download PDFInfo
- Publication number
- EP0943881B1 EP0943881B1 EP98104947A EP98104947A EP0943881B1 EP 0943881 B1 EP0943881 B1 EP 0943881B1 EP 98104947 A EP98104947 A EP 98104947A EP 98104947 A EP98104947 A EP 98104947A EP 0943881 B1 EP0943881 B1 EP 0943881B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- bed
- flow resistance
- height
- cooled
- conveying speed
- 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
Classifications
-
- 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
- F27D15/00—Handling or treating discharged material; Supports or receiving chambers therefor
- F27D15/02—Cooling
- F27D15/0206—Cooling with means to convey the charge
- F27D15/0213—Cooling with means to convey the charge comprising a cooling grate
-
- 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
Definitions
- grate coolers for fuel for example for cooling cement clinker
- the effectiveness of grate coolers for fuel is of the uniformity of the Rust occupancy dependent on the refrigerated goods. Is the thickness of the Gutbetts unevenly, so it is from below through the grate driven cooling air mainly those areas of the material bed flow through a smaller thickness and consequently a have lower flow resistance.
- the Layer height is determined, for example, by means of gamma radiation meters ("ZEMENT-LALK-GIPS" 1967, 152-156) or about the weight the grate occupancy (DE-A-195 41 455) determined. It is also proposed been the conveying speed of the cooling grate depending on the flow resistance in the initial area of the same to regulate (US-A-2 084 976; "CEMENT-LIME-GYPSUM” 1974, 559-564).
- the invention improves the cooler operation in that the Conveying speed depends on both the height of the refrigerated goods bed as well as the flow resistance becomes.
- Another advantage of the invention is that when The conveyor movement falls below a minimum clinker bed height the rust can be stopped. In the event of business interruptions is caused by the rust also in the initial area is covered with good. This prevents that hot goods when restarting on the unprotected grate falls, and the thermal load on the grate plates when restarting is reduced.
- the invention leads to an equalization of the grate occupancy and a better economic use of cooling air due to the lower fluctuation in the temperature of the secondary air fed into the furnace.
- the height of the refrigerated goods bed is the more important Influencing variable is. Therefore, it preferably gets stronger acted as the flow resistance. In practice, this can be achieved in that the Height of the refrigerated goods bed as a reference variable and the flow resistance used as a disturbance variable or correction variable becomes.
- the current flow resistance not or not exclusively used immediately, but instead or additionally its first derivative or its deviation from Long-term value.
- the flow resistance and / or its first derivative are therefore used as a correction variable based on the clinker bed height specified setpoint of the conveying speed, to influence the grain on the heat transfer compensate and an almost constant energy return in the oven and, if necessary, an equalization of the To allow heat exchange. If the pressure resistance in the Clinker, the target value of the clinker bed height is correctively increased, to improve heat exchange. If the Pressure resistance in the refrigerated goods bed becomes the setpoint for the bed height decreased to keep the heat exchange at a constant level to keep.
- the flow resistance is also possible to consider the flow resistance as Use the reference variable and the layer height as a correction variable. Furthermore, the change in time can also occur in both cases the layer height can be included in the regulation.
- the term rules means first Line in line with common terminology influencing the conveying speed in closed Control loop.
- the interference is said to be more open Loop that is commonly referred to as taxes not be excluded.
- the radiator for example, known radars are suitable.
- the flow resistance in the initial area of the cooler results from the constant regulated used there Cooling air volume and the resulting differential pressure between the supplied air and the grate top space or (simplifying) from the counter pressure.
- the conveying speed of a cooling grate's sliding grate Cement clinker is to be regulated so that a layer height of 600 mm, if there is a value of the flow resistance is measured, which corresponds to this layer height as normal was predetermined, for example 60 mbar. Is at this layer height a lower flow resistance measured, for example 50 mbar, the controller changes the Target value of the layer height to 650 mm.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Furnace Details (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
- Paper (AREA)
- Control Of Temperature (AREA)
- Coke Industry (AREA)
Abstract
Description
Die Wirksamkeit von Rostkühlern für Brenngut, beispielsweise zum Kühlen von Zementklinker, ist von der Gleichmäßigkeit der Rostbelegung durch das Kühlgut abhängig. Ist die Dicke des Gutbetts ungleichmäßig, so wird die von unten durch den Rost getriebene Kühlluft vorwiegend diejenigen Bereiche des Gutbetts durchströmen, die eine geringere Dicke und folglich einen geringeren Durchströmungswiderstand haben. Die Bereiche, in denen die Dicke des Kühlgutbetts größer ist, werden gegebenenfalls unzureichend gekühlt bzw. es muß ein größerer Kühlaufwand getrieben werden, um eine hinreichende Abkühlung selbst in den schwächer durchströmten Bereichen des Gutbetts zu erzielen. Da der Abwurf des zu kühlenden Brennguts aus dem vorgeschaltenen Ofen in den Anfangsbereich des Kühlers in der Regel nicht völlig gleichmäßig erfolgt, muß mit ungleichmäßiger Rostbelegung gerechnet werden.The effectiveness of grate coolers for fuel, for example for cooling cement clinker, is of the uniformity of the Rust occupancy dependent on the refrigerated goods. Is the thickness of the Gutbetts unevenly, so it is from below through the grate driven cooling air mainly those areas of the material bed flow through a smaller thickness and consequently a have lower flow resistance. The areas, in which the thickness of the refrigerated goods bed is greater, if necessary insufficiently cooled or a larger one must be used Cooling efforts are driven to ensure adequate cooling even in the areas of the estate bed with less flow to achieve. Since the dropping of the kiln to be cooled from the upstream furnace in the initial area of the cooler in the Usually not done completely evenly, must be done with uneven Rust occupancy can be expected.
Zur Vermeidung dieses Nachteils ist es bekannt, die Höhe der Kühlgutschicht im Anfangsabschnitt des Rosts zu messen und die Fördergeschwindigkeit des Rosts so zu regeln, daß eine möglichst gleichmäßige Schichthöhe erreicht wird. Die Schichthöhe wird beispielsweise mittels Gammastrahlungsmessern ("ZEMENT-KALK-GIPS" 1967, 152-156) oder über das Gewicht der Rostbelegung (DE-A-195 41 455) bestimmt. Ferner ist vorgeschlagen worden, die Fördergeschwindigkeit des Kühlrosts abhängig vom Durchströmungswiderstand im Anfangsbereich desselben zu regeln (US-A-2 084 976; "ZEMENT-KALK-GIPS" 1974, 559-564). In Perioden geringen Kühlgutanfalls, die bei konstanter Fördergeschwindigkeit zu Bereichen geringer Rostbelegung führen würden, wird die Fördergeschwindigkeit des Rosts verringert, in Perioden verstärkten Kühlgutanfalls verfährt man umgekehrt. Jedoch hat sich erwiesen, daß die auf diese Weise erzielbare Verbesserung sehr begrenzt ist. Das liegt daran, daß der Durchströmungswiderstand nicht nur von der Dicke des Kühlgutbetts abhängt, sondern auch von dessen Korngrößenverteilung, die gleichfalls mit Schwankungen des Ofenbetriebs unterschiedlich ausfallen kann. Je gröber das Klinkerkorn ist, um so geringer ist bei gleicher Höhe des Kühlgutbetts der Durchströmungswiderstand. Wenn beispielsweise grobe Ofenansatzbrocken anfallen, ist der gemessene Durchströmungswiderstand vergleichsweise gering, was bei durchströmungsabhängiger Regelung zu einer Verringerung der Fördergeschwindigkeit des Kühlrosts führt mit der Gefahr der Überfüllung des Rosts.To avoid this disadvantage, it is known the amount of To measure the refrigerated goods layer in the initial section of the grate and regulate the conveying speed of the grate so that a layer height which is as uniform as possible is achieved. The Layer height is determined, for example, by means of gamma radiation meters ("ZEMENT-LALK-GIPS" 1967, 152-156) or about the weight the grate occupancy (DE-A-195 41 455) determined. It is also proposed been the conveying speed of the cooling grate depending on the flow resistance in the initial area of the same to regulate (US-A-2 084 976; "CEMENT-LIME-GYPSUM" 1974, 559-564). In periods low volume of refrigerated goods at a constant conveying speed would lead to areas with little rust, the conveying speed of the grate is reduced, in Periods of increased chilled goods are reversed. However, it has been shown that the achievable in this way Improvement is very limited. This is because the Flow resistance not only from the thickness of the refrigerated goods bed depends, but also on its grain size distribution, which also varies with fluctuations in furnace operation can fail. The coarser the clinker grain, um the lower the flow resistance for the same height of the refrigerated goods bed. If, for example, coarse lumps of kiln is the measured flow resistance comparatively low, what with flow-dependent control to reduce the conveying speed of the Cooling grate leads to the risk of overfilling the grate.
Die Erfindung verbessert den Kühlerbetrieb dadurch, daß die Fördergeschwindigkeit abhängig sowohl von der Höhe des Kühlgutbetts als auch des Durchströmungswiderstands geregelt wird.The invention improves the cooler operation in that the Conveying speed depends on both the height of the refrigerated goods bed as well as the flow resistance becomes.
Durch den Einfluß der Höhe des Kühlgutbetts werden die Schwächen, die bei alleiniger Berücksichtigung des Durchströmungswiderstands unvermeidlich sind, reduziert. So wird in dem soeben genannten Beispiel des Anfalls grober Ofenansatzbrocken die Messung einer entsprechend großen Höhe des Kühlgutbetts die Tendenz zu einer Beschleunigung der Fördergeschwindigkeit bewirken, durch die der gegensinnige Einfluß des geringeren Durchströmungswiderstands zumindest wettgemacht wird. Es wird vermieden, daß der Kühlereinlaufschacht mit groben Ofenansatzbrocken überfüllt und der Antrieb des Kühlerrosts überlastet werden könnte, was einen Ofenstillstand zur Folge hätte.Due to the influence of the height of the refrigerated goods bed, the weaknesses, taking into account the flow resistance alone are inevitable, reduced. So it just happens in that mentioned example of the production of coarse chunks of kiln the measurement of a correspondingly large height of the refrigerated goods bed the tendency to accelerate the conveying speed by which the opposing influence of the lesser Flow resistance is at least made up for. It will avoided that the radiator inlet shaft with coarse chunks of furnace overfilled and the drive of the grille overloaded could be, which would result in a furnace shutdown.
Ein weiterer Vorteil der Erfindung besteht darin, daß beim Unterschreiten einer Mindestklinkerbetthöhe die Förderbewegung des Rosts gestoppt werden kann. Im Falle von Betriebsunterbrechungen wird dadurch bewirkt, daß der Rost auch im Anfangsbereich mit Gut bedeckt ist. Dadurch wird verhindert, daß heißes Gut beim Wiederanfahren auf den ungeschützten Rost fällt, und die thermische Belastung der Rostplatten beim Wiederanfahren wird vermindert.Another advantage of the invention is that when The conveyor movement falls below a minimum clinker bed height the rust can be stopped. In the event of business interruptions is caused by the rust also in the initial area is covered with good. This prevents that hot goods when restarting on the unprotected grate falls, and the thermal load on the grate plates when restarting is reduced.
Die Erfindung führt zu einer Vergleichmäßigung der Rostbelegung und zu einer wärmewirtschaftlich besseren Kühlluftausnutzung infolge der geringeren Schwankung der Temperatur der in den Ofen geführten Sekundärluft.The invention leads to an equalization of the grate occupancy and a better economic use of cooling air due to the lower fluctuation in the temperature of the secondary air fed into the furnace.
Es hat sich gezeigt, daß die Höhe des Kühlgutbetts die wichtigere Einflußgröße ist. Sie wird deswegen vorzugsweise stärker zur Einwirkung gebracht als der Durchströmungswiderstand. In der Praxis kann dies dadurch verwirklicht werden, daß die Höhe des Kühlgutbetts als Führungsgröße und der Durchströmungswiderstand als Störgröße bzw. Korrekturgröße verwendet wird. Bei einer besonders vorteilhaften Ausführungsform wird der momentane Durchströmungswiderstand nicht oder nicht ausschließlich unmittelbar eingesetzt, sondern statt dessen oder zusätzlich seine erste Ableitung oder seine Abweichung vom Langzeitwert.It has been shown that the height of the refrigerated goods bed is the more important Influencing variable is. Therefore, it preferably gets stronger acted as the flow resistance. In practice, this can be achieved in that the Height of the refrigerated goods bed as a reference variable and the flow resistance used as a disturbance variable or correction variable becomes. In a particularly advantageous embodiment the current flow resistance not or not exclusively used immediately, but instead or additionally its first derivative or its deviation from Long-term value.
Der Durchströmungswiderstand und/oder seine erste Ableitung werden somit als Korrekturgröße auf den von der Klinkerbetthöhe vorgegebenen Sollwert der Fördergeschwindigkeit aufgeschaltet, um den Körnungseinfluß auf den Wärmeübergang zu kompensieren und eine annähernd konstante Energierückführung in den Ofen und gegebenenfalls eine Vergleichmäßigung des Wärmeaustauschs zu ermöglichen. Sinkt der Druckwiderstand im Klinker, wird der Sollwert der Klinkerbetthöhe korrektiv angehoben, um den Wärmeaustausch zu verbessern. Steigt der Druckwiderstand im Kühlgutbett, wird der Sollwert der Betthöhe vermindert, um den Wärmeaustausch auf einem konstanten Niveau zu halten.The flow resistance and / or its first derivative are therefore used as a correction variable based on the clinker bed height specified setpoint of the conveying speed, to influence the grain on the heat transfer compensate and an almost constant energy return in the oven and, if necessary, an equalization of the To allow heat exchange. If the pressure resistance in the Clinker, the target value of the clinker bed height is correctively increased, to improve heat exchange. If the Pressure resistance in the refrigerated goods bed becomes the setpoint for the bed height decreased to keep the heat exchange at a constant level to keep.
Jedoch ist es auch möglich, den Durchströmungswiderstand als Führungsgröße und die Schichthöhe als Korrekturgröße zu verwenden. Ferner kann auch in beiden Fällen die zeitliche Änderung der Schichthöhe in die Regelung einbezogen werden. However, it is also possible to consider the flow resistance as Use the reference variable and the layer height as a correction variable. Furthermore, the change in time can also occur in both cases the layer height can be included in the regulation.
Der Begriff Regeln meint im vorliegenden Zusammenhang in erster Linie in Übereinstimmung mit der üblichen Terminologie die Beeinflussung der Fördergeschwindigkeit in geschlossener Regelschleife. Jedoch soll die Beeinflussung in offener Schleife, die üblicherweise als Steuern bezeichnet wird, dadurch nicht ausgeschlossen sein.In the present context, the term rules means first Line in line with common terminology influencing the conveying speed in closed Control loop. However, the interference is said to be more open Loop that is commonly referred to as taxes not be excluded.
Für die Messung der Höhe des Kühlgutbetts im Anfangsbereich des Kühlers eignen sich beispielsweise bekannte Radargeräte. Der Durchströmungswiderstand im Anfangsbereich des Kühlers ergibt sich aus dem dort eingesetzten konstant geregelten Kühlluftvolumen und dem sich dabei ergebenden Differenzdruck zwischen der zugeführten Luft und dem Rostoberraum oder (vereinfachend) aus dem Gegendruck.For measuring the height of the refrigerated goods bed in the initial area the radiator, for example, known radars are suitable. The flow resistance in the initial area of the cooler results from the constant regulated used there Cooling air volume and the resulting differential pressure between the supplied air and the grate top space or (simplifying) from the counter pressure.
Unter der Fördergeschwindigkeit ist im vorliegenden Zusammenhang die Geschwindigkeit der Rostbewegung zu verstehen. Bei einem Schubrost entspricht diese dem Produkt aus Schublänge und Frequenz der oszillierenden Schubbewegung. Sie kann von der Transportgeschwindigkeit des darauf befindlichen Kühlgutbetts abweichen.Under the conveyor speed is in the present context understand the speed of the rust movement. at a sliding grate corresponds to the product of drawer length and frequency of the oscillating thrust movement. It can from the transport speed of the refrigerated goods bed on it differ.
Die Fördergeschwindigkeit des Schubrosts eines Kühlers für Zementklinker ist so zu regeln, daß sich eine Schichthöhe von 600 mm ergibt, sofern dabei ein Wert des Durchströmungswiderstands gemessen wird, der dieser Schichthöhe als normal entsprechend vorbestimmt wurde, beispielsweise 60 mbar. Wird bei dieser Schichthöhe ein geringerer Durchströmungswiderstand gemessen, beispielsweise 50 mbar, so ändert der Regler den Sollwert der Schichthöhe auf 650 mm.The conveying speed of a cooling grate's sliding grate Cement clinker is to be regulated so that a layer height of 600 mm, if there is a value of the flow resistance is measured, which corresponds to this layer height as normal was predetermined, for example 60 mbar. Is at this layer height a lower flow resistance measured, for example 50 mbar, the controller changes the Target value of the layer height to 650 mm.
Claims (4)
- Method of controlling the conveying speed of a grate cooler as a function of the state of the bed of material to be cooled in the initial region of the cooler while taking into account the flow resistance, characterized in that the conveying speed is controlled as a function of both the height of the bed of material to be cooled and the flow resistance in the initial region of the cooler, namely with the tendency of the conveying speed to accelerate when a large height of the layer of material to be cooled is determined, and vice versa, and also with the tendency of the conveying speed to accelerate when a large flow resistance is determined, and vice versa.
- Method according to Claim 1, characterized in that the height of the bed of material to be cooled is used as reference variable and the flow resistance is used as correcting variable.
- Method according to Claim 2, characterized in that, for the control of the conveying speed, instead of the flow resistance or the height of the bed of material to be cooled, or in addition to the flow resistance or the height of the bed of material to be cooled, the change per unit time in the flow resistance or in the height of the bed of material to be cooled is used.
- Method according to Claim 2, characterized in that, for the control of the conveying speed, instead of the flow resistance and/or the height of the bed of material to be cooled, or in addition to the flow resistance or in addition to the height of the bed of material to be cooled, the deviation of the flow resistance or of the height of the bed of material to be cooled from their long-time value is used.
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP98104947A EP0943881B1 (en) | 1998-03-18 | 1998-03-18 | Control process of the conveyance speed in a travelling grate cooler |
DE59811795T DE59811795D1 (en) | 1998-03-18 | 1998-03-18 | Process for regulating the conveying speed of a grate cooler |
DK98104947T DK0943881T3 (en) | 1998-03-18 | 1998-03-18 | Method for regulating the transport speed of a grate cooler |
AT98104947T ATE273498T1 (en) | 1998-03-18 | 1998-03-18 | METHOD FOR CONTROLLING THE CONVEYING SPEED OF A GRATE COOLER |
US09/271,681 US6036483A (en) | 1998-03-18 | 1999-03-18 | Method of controlling the conveying speed of a grate cooler |
JP07379699A JP4402760B2 (en) | 1998-03-18 | 1999-03-18 | Control method of transfer speed of lattice cooler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP98104947A EP0943881B1 (en) | 1998-03-18 | 1998-03-18 | Control process of the conveyance speed in a travelling grate cooler |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0943881A1 EP0943881A1 (en) | 1999-09-22 |
EP0943881B1 true EP0943881B1 (en) | 2004-08-11 |
Family
ID=8231609
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP98104947A Expired - Lifetime EP0943881B1 (en) | 1998-03-18 | 1998-03-18 | Control process of the conveyance speed in a travelling grate cooler |
Country Status (6)
Country | Link |
---|---|
US (1) | US6036483A (en) |
EP (1) | EP0943881B1 (en) |
JP (1) | JP4402760B2 (en) |
AT (1) | ATE273498T1 (en) |
DE (1) | DE59811795D1 (en) |
DK (1) | DK0943881T3 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104833234A (en) * | 2014-02-10 | 2015-08-12 | 山西太钢不锈钢股份有限公司 | Method for controlling dynamic balance of level of material bin in sintering process of sintering machine |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE202004020574U1 (en) * | 2003-05-08 | 2005-08-11 | Claudius Peters Technologies Gmbh | Process for treating, especially cooling, a bulk material layer uses a gas stream on a grid consisting of panels driven forward and backward in the conveying direction |
DE102004054417B4 (en) * | 2004-11-11 | 2014-02-20 | Khd Humboldt Wedag Gmbh | Method for controlling the operation of a bulk material cooler |
DE102005032518B4 (en) * | 2005-07-12 | 2017-10-19 | Thyssenkrupp Industrial Solutions Ag | Method and device for cooling bulk material |
DE102007019530C5 (en) * | 2007-04-25 | 2018-01-04 | Alite Gmbh | Method and device for cooling a bulk material layer lying on a conveyor grate |
DE202013005996U1 (en) | 2013-06-27 | 2013-07-24 | Khd Humboldt Wedag Gmbh | Clinker cooler with grate for the separation of large clinker dross |
DE102014000255B4 (en) | 2014-01-08 | 2018-03-01 | Khd Humboldt Wedag Gmbh | Method for controlling the efficiency of a bulk material cooler |
CN103808160B (en) * | 2014-01-26 | 2016-02-03 | 浙江邦业科技股份有限公司 | Based on the thickness of feed layer characterizing method of grate-cooler hydraulic pressure |
CN105447252B (en) * | 2015-12-01 | 2018-10-16 | 中信重工机械股份有限公司 | A kind of computational methods of pusher bar type hydraulic system of grate cooler type selecting |
BE1027669B1 (en) * | 2019-10-14 | 2021-05-12 | Thyssenkrupp Ind Solutions Ag | Method and cooler for cooling bulk goods, in particular cement clinker |
WO2021074059A1 (en) * | 2019-10-14 | 2021-04-22 | Thyssenkrupp Industrial Solutions Ag | Cooler for cooling bulk material |
BE1027678B1 (en) * | 2019-10-14 | 2021-05-12 | Thyssenkrupp Ind Solutions Ag | Cooler for cooling bulk goods |
DE102019215771A1 (en) * | 2019-10-14 | 2021-04-15 | Thyssenkrupp Ag | Cooler for cooling bulk goods |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2031047A (en) * | 1932-02-13 | 1936-02-18 | Harry S Lee | Apparatus for manufacturing, treating, and cooling cement clinkers |
US2055941A (en) * | 1932-08-22 | 1936-09-29 | Allis Chalmers Mfg Co | Cooler |
US2084976A (en) * | 1933-08-30 | 1937-06-22 | Allis Chalmers Mfg Co | Speed controller for clinker coolers |
US3064357A (en) * | 1959-09-02 | 1962-11-20 | Industrial Nucleonics Corp | Conveyor speed control by measuring material level |
DE1408996B2 (en) * | 1960-09-24 | 1970-09-10 | Rheinische Kalksteinwerke GmbH, 5603 Wulfrath | Method for the automatic control of a traveling grate cooler |
US3236358A (en) * | 1961-05-19 | 1966-02-22 | Allis Chalmers Mfg Co | Means for controlling conveyer |
DD104354A1 (en) * | 1972-06-26 | 1974-03-05 | ||
US3929219A (en) * | 1974-03-27 | 1975-12-30 | Dravo Corp | Reciprocating variable speed material transfer conveyor system |
US4170183A (en) * | 1977-10-20 | 1979-10-09 | Energy Generation, Inc. | Incinerating method and apparatus having selective, controlled movement of materials during combustion |
DE4003679A1 (en) * | 1990-02-07 | 1991-08-22 | Krupp Polysius Ag | METHOD AND DEVICE FOR COOLING BURNED BULLET |
JP3085325B2 (en) * | 1992-05-20 | 2000-09-04 | 住友大阪セメント株式会社 | Clinker cooler control device and control method |
-
1998
- 1998-03-18 DK DK98104947T patent/DK0943881T3/en active
- 1998-03-18 AT AT98104947T patent/ATE273498T1/en not_active IP Right Cessation
- 1998-03-18 DE DE59811795T patent/DE59811795D1/en not_active Expired - Fee Related
- 1998-03-18 EP EP98104947A patent/EP0943881B1/en not_active Expired - Lifetime
-
1999
- 1999-03-18 JP JP07379699A patent/JP4402760B2/en not_active Expired - Fee Related
- 1999-03-18 US US09/271,681 patent/US6036483A/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104833234A (en) * | 2014-02-10 | 2015-08-12 | 山西太钢不锈钢股份有限公司 | Method for controlling dynamic balance of level of material bin in sintering process of sintering machine |
CN104833234B (en) * | 2014-02-10 | 2016-08-24 | 山西太钢不锈钢股份有限公司 | A kind of sintering machine sintering process material bin dynamic equilibrium control method |
Also Published As
Publication number | Publication date |
---|---|
US6036483A (en) | 2000-03-14 |
ATE273498T1 (en) | 2004-08-15 |
JP2000065331A (en) | 2000-03-03 |
EP0943881A1 (en) | 1999-09-22 |
DE59811795D1 (en) | 2004-09-16 |
JP4402760B2 (en) | 2010-01-20 |
DK0943881T3 (en) | 2005-01-03 |
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