EP0154690A2 - Regulation of a fluidised-bed combustion apparatus in a heating boiler - Google Patents
Regulation of a fluidised-bed combustion apparatus in a heating boiler Download PDFInfo
- Publication number
- EP0154690A2 EP0154690A2 EP84114617A EP84114617A EP0154690A2 EP 0154690 A2 EP0154690 A2 EP 0154690A2 EP 84114617 A EP84114617 A EP 84114617A EP 84114617 A EP84114617 A EP 84114617A EP 0154690 A2 EP0154690 A2 EP 0154690A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- temperature
- fuel
- fluidized bed
- bed
- supply
- 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.)
- Withdrawn
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C10/00—Fluidised bed combustion apparatus
- F23C10/18—Details; Accessories
- F23C10/28—Control devices specially adapted for fluidised bed, combustion apparatus
-
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N2225/00—Measuring
- F23N2225/08—Measuring temperature
- F23N2225/16—Measuring temperature burner temperature
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N2233/00—Ventilators
- F23N2233/06—Ventilators at the air intake
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N2239/00—Fuels
- F23N2239/02—Solid fuels
Definitions
- the invention relates to a regulation according to the preamble of claim 1.
- Fluidized bed firing swirls and burns fine-grained fuel. Such furnaces are particularly suitable for burning coal rich in ballast. In addition to the use in large-scale plants, fluidized bed furnaces are also becoming increasingly interesting for water heaters and heating boilers. The advantages of this type of firing can be put to excellent use here.
- Precise control is essential for the functioning of the fluidized bed furnaces. Since it is a solid fuel firing, several aspects have to be considered. In addition to the usual criteria, such as setting and maintaining the correct bed temperature, there is also a dependency on the heat requirement when using fluidized bed firing in heating boilers.
- the object of the invention was to set and maintain the correct bed temperature and also to take into account the heat demand from the boiler water.
- the controlled variable is used to determine the bed temperature using temperature sensors in the fluidized bed. These ensure that the required bed temperature is set and maintained, including safety monitoring.
- the required bed temperature is first achieved by switching on the forced draft burner. At a lower switching point, the actual fluidized bed combustion is switched over. An upper switching point is used to monitor the maximum bed temperature. The fuel supply is interrupted until a lower limit temperature is reached.
- the flow temperature determined by a flow thermostat, serves as a further control variable. If heat is requested when the flow temperature falls below the target value, the induced draft and combustion air fan are switched on and the air control flap is opened. Then fuel is added. As a result, there is sufficient heat replenishment through the fluidized bed even if the fuel supply through the thermostats in the fluidized bed should be cut off. As soon as the target flow temperature is exceeded again, the fuel supply is shut off. The combustion air fan and suction run on first. To the air control flap is closed when it is switched off. The bed temperature is therefore not raised to the maximum temperature.
- the mouth area of the fuel conveyor preferably a fuel feed screw, must be particularly protected against overheating with the risk of reignition.
- an air valve is opened after the fuel supply is shut off and the mouth area is blown free of ash and coal residues. If a specified maximum temperature is nevertheless exceeded, the coal dosing screw under the bunker is stopped and lime or sand is added as a coolant on the short side.
- the pressure in the fluidized bed is continuously monitored during the actual fluidized bed operation. Pressure overshoots and undershoots are signaled. Since the formation of ash changes the pressure in the fluidized bed, it is possible to control the ash extraction depending on the pressure.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Abstract
Description
Die Erfindung betrifft eine Regelung nach dem Oberbegriff des Patentanspruches 1.The invention relates to a regulation according to the preamble of claim 1.
Bei Wirbelschichtfeuerungen wird feinkörmiger Brennstoff verwirbelt und verbrannt. Solche Feuerungen sind besonders zum Verfeuern von balastreicher Kohle geeignet. Neben dem Einsatz in großtechnischen Anlagen werden Wirbelschichtfeuerungen auch immer stärker für Wassererhitzer wie Heizungskessel interessant. Hier lassen sich die Vorzüge dieser Feuerungsart hervorragend nutzen.Fluidized bed firing swirls and burns fine-grained fuel. Such furnaces are particularly suitable for burning coal rich in ballast. In addition to the use in large-scale plants, fluidized bed furnaces are also becoming increasingly interesting for water heaters and heating boilers. The advantages of this type of firing can be put to excellent use here.
Von wesentlicher Bedeutung für die Funktion der Wirbelschichtfeuerungen ist eine genaue Regelung. Da es sich um eine Feststoff-Feuerung handelt, müssen mehrere Gesichtspunkte berücksichtigt werden. Neben den üblichen Kriterien, wie dem Einstellen und Einhalten der richtigen Bett-Temperatur kommt bei der Verwendung der Wirbelschichtfeuerung in Heizungskesseln noch die Abhängigkeit von der Wärmeanforderung hinzu.Precise control is essential for the functioning of the fluidized bed furnaces. Since it is a solid fuel firing, several aspects have to be considered. In addition to the usual criteria, such as setting and maintaining the correct bed temperature, there is also a dependency on the heat requirement when using fluidized bed firing in heating boilers.
Der Erfindung lag die Aufgabe zugrunde, die richtige Bett-Temperatur einzustellen und einzuhalten und dabei zusätzlich die Wärmeanforderung durch das Kesselwasser zu berücksichtigen.The object of the invention was to set and maintain the correct bed temperature and also to take into account the heat demand from the boiler water.
Gemäß der Erfindung wird dieses erreicht durch die im Kennzeichen des Patentanspruches 1 genannten Maßnahmen.According to the invention, this is achieved by the measures mentioned in the characterizing part of claim 1.
Als Regelgröße dient auf der einen Seite die Bett-Temperatur ermittel durch Temperaturfühler im Wirbelbett. Diese sorgen für das Einstellen und Einhalten der erforderlichen Bett-Temperatur einschließlich einer Sicherheitsüberwachung. Durch Einschalten des Gebläsebrenners wird zunächst die erforderliche Bett-Temperatur erzielt. Bei einem unteren Schaltpunkt wird dann auf die eigentliche Wirbelschichtfeuerung umgeschaltet. Der Überwachung der maximalen Bett-Temperatur dient ein oberer Schaltpunkt. Bei diesem wird die Brennstoffzufuhr unterbrochen bis eine untere Grenztemperatur erreicht ist.On the one hand, the controlled variable is used to determine the bed temperature using temperature sensors in the fluidized bed. These ensure that the required bed temperature is set and maintained, including safety monitoring. The required bed temperature is first achieved by switching on the forced draft burner. At a lower switching point, the actual fluidized bed combustion is switched over. An upper switching point is used to monitor the maximum bed temperature. The fuel supply is interrupted until a lower limit temperature is reached.
Als weitere Regelgröße dient die Vorlauftemperatur ermittelt durch einen Vorlaufthermostaten. Wird bei unterschrittener Soll-Vorlauftemperatur Wärme angefordert, dann werden zunächst Saugzug und Verbrennungsluftventilator eingeschaltet und die Luftregelklappe geöffnet. Anschließend wird Brennstoff zugeführt. Dadurch erfolgt ein ausreichender Wärmenachschub durch das Wirbelbett selbst dann, wenn die Brennstoffzufuhr durch die Thermostate im Wirbelbett unterborchen sein sollte. Sobald die Soll-Vorlauftemperatur wieder überschritten wird, wird die Brennstoffzufuhr abgesperrt.Verbrennungsluftventilator und Saugzug laufen zunächst nach. Nach ihrer Abschaltung wird die Luftregelklappe geschlossen. Die Bett-Temperatur wird also nicht bis zur maximalen Temperatur hochgefahren.The flow temperature, determined by a flow thermostat, serves as a further control variable. If heat is requested when the flow temperature falls below the target value, the induced draft and combustion air fan are switched on and the air control flap is opened. Then fuel is added. As a result, there is sufficient heat replenishment through the fluidized bed even if the fuel supply through the thermostats in the fluidized bed should be cut off. As soon as the target flow temperature is exceeded again, the fuel supply is shut off. The combustion air fan and suction run on first. To the air control flap is closed when it is switched off. The bed temperature is therefore not raised to the maximum temperature.
Sollte während der Stillstandsphase, d.h. bei abgeschalteter Luft- und Brennstoffzufuhr, die maximale Bettemperatur überschritten werden, dann wird über einen Temperaturfühler im Wirbelbett die Luftzufuhr bis zum Erreichen der unteren Grenztemperatur freigegeben. Das erfolgt im konkreten Fall durch Einschalten von Saugzug und Verbrennungsluftventilator und Öffnen der Luftregelklappe. Es ist somit ein Schutz gegen Überhitzung vor, handen.Should during the standstill phase, i.e. If the air and fuel supply is switched off, the maximum bed temperature is exceeded, then the air supply is released via a temperature sensor in the fluidized bed until the lower limit temperature is reached. In this specific case, this is done by switching on the induced draft and combustion air fan and opening the air control flap. It is therefore a protection against overheating.
Der Mündungsbereich des Brennstoff-Förderers, vorzugsweise einer Brennstoffeintragschnecke, muß besonders gegen Überhitzung mit der Gefahr einer Rückzündung geschützt werden. Zu diesem Zweck wird nach dem Absperren der Brennstoffzufuhr ein Luftventil geöffnet und der Mündungsbereich von Asche und Kohleresten freigeblasen. Sollte dennoch eine festgelegte Höchsttemperatur überschritten werden, dann wird die Kohledosierschnecke unter dem Bunker angehalten und dafür kurzseitig Kalk oder Sand als Kühlmittel zugegeben.The mouth area of the fuel conveyor, preferably a fuel feed screw, must be particularly protected against overheating with the risk of reignition. For this purpose, an air valve is opened after the fuel supply is shut off and the mouth area is blown free of ash and coal residues. If a specified maximum temperature is nevertheless exceeded, the coal dosing screw under the bunker is stopped and lime or sand is added as a coolant on the short side.
Während des eigentlichen Wirbelschichtbetriebes wird der Druck im Wirbelbett kontinuierlich überwacht. Drucküber-und -unterschreitungen werden signalisiert. Da die Aschebildung den Druck im Wirbelbett verändert, besteht die Möglichkeit den Ascheabzug druckabhängig zu steuern.The pressure in the fluidized bed is continuously monitored during the actual fluidized bed operation. Pressure overshoots and undershoots are signaled. Since the formation of ash changes the pressure in the fluidized bed, it is possible to control the ash extraction depending on the pressure.
Claims (5)
dadurch gekennzeichnet, daß über Temperaturfühler im Wirbelbett mit mehreren Schaltpunkten
und daß ferner über einen Thermostaten im Vorlauf
characterized in that via temperature sensors in the fluidized bed with several switching points
and that also via a thermostat in advance
dadurch gekennzeichnet, daß über einen Temperaturfühler im Wirbelbett bei Überschreiten der maximalen Bett-Temperatur während der Stillstandsphase die Luftzufuhr bis zum Erreichen einer unteren Grenztemperatur freigegeben wird.2. Regulation according to claim 1,
characterized in that the air supply is released until a lower limit temperature is reached via a temperature sensor in the fluidized bed when the maximum bed temperature is exceeded during the standstill phase.
dadurch gekennzeichnet, daß nach dem Absperren der Brennstoffzufuhr durch öffnen eines Ventiles der Mündungsbereich des Brennstoff-Förderers freigeblasen wird.3. Regulation according to claim 1,
characterized in that after the fuel supply has been shut off, the opening area of the fuel conveyor is blown free by opening a valve.
dadurch gekennzeichnet, daß über einen Temperaturfühler an der Mündung des Brennstoff-Förderers bei Überschreiten einer festgelegten Höchsttemperatur kurzzeitig die Zufuhr von Kalk oder Sand als Kühlmittel eingeschaltet wird.4. Regulation according to claims 1 to 3,
characterized in that the supply of lime or sand as a coolant is briefly switched on via a temperature sensor at the mouth of the fuel conveyor when a predetermined maximum temperature is exceeded.
dadurch gekennzeichnet, daß ab Erreichen der erforderlichen Bett-Temperatur der Differenzdruck des Wirbelbettes überwacht und oberhalb eines festgelegten Druckes der Ascheabzug eingeschaltet wird.5. Regulation according to claim 1,
characterized in that when the required bed temperature is reached, the differential pressure of the fluidized bed is monitored and the ash extraction is switched on above a predetermined pressure.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3407132 | 1984-02-28 | ||
DE19843407132 DE3407132A1 (en) | 1984-02-28 | 1984-02-28 | CONTROL OF A FLUIDIZED BURN FIRING IN A HEATING BOILER |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0154690A2 true EP0154690A2 (en) | 1985-09-18 |
EP0154690A3 EP0154690A3 (en) | 1986-03-19 |
Family
ID=6229000
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP84114617A Withdrawn EP0154690A3 (en) | 1984-02-28 | 1984-12-01 | Regulation of a fluidised-bed combustion apparatus in a heating boiler |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP0154690A3 (en) |
DE (1) | DE3407132A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106224947A (en) * | 2016-08-04 | 2016-12-14 | 华北电力大学 | The event-driven control system of Circulating Fluidized Bed Temperature based on feedback of status |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1526061A1 (en) * | 1964-03-31 | 1969-09-25 | Dorr Oliver Inc | Process and device for the incineration of organic waste with a high moisture content |
US3508506A (en) * | 1968-06-13 | 1970-04-28 | Us Interior | Process and apparatus for reduction of unburned combustible in fly ash |
JPS5541365A (en) * | 1978-09-18 | 1980-03-24 | Ishigaki Kiko Kk | Method of and apparatus for removing foreign matter from fluidized furnace |
EP0028458A2 (en) * | 1979-10-03 | 1981-05-13 | Sandfire (Proprietary) Limited | Fluidised-bed boilers |
US4295817A (en) * | 1978-08-04 | 1981-10-20 | The Energy Equipment Co. Ltd. | Method and means for controlling the operation of fluidized bed combustion apparatus |
US4416418A (en) * | 1982-03-05 | 1983-11-22 | Goodstine Stephen L | Fluidized bed residential heating system |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DK155464C (en) * | 1978-10-27 | 1989-08-21 | Smidth & Co As F L | WHIRL CHAMBER BRANCH SYSTEM |
-
1984
- 1984-02-28 DE DE19843407132 patent/DE3407132A1/en not_active Ceased
- 1984-12-01 EP EP84114617A patent/EP0154690A3/en not_active Withdrawn
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1526061A1 (en) * | 1964-03-31 | 1969-09-25 | Dorr Oliver Inc | Process and device for the incineration of organic waste with a high moisture content |
US3508506A (en) * | 1968-06-13 | 1970-04-28 | Us Interior | Process and apparatus for reduction of unburned combustible in fly ash |
US4295817A (en) * | 1978-08-04 | 1981-10-20 | The Energy Equipment Co. Ltd. | Method and means for controlling the operation of fluidized bed combustion apparatus |
JPS5541365A (en) * | 1978-09-18 | 1980-03-24 | Ishigaki Kiko Kk | Method of and apparatus for removing foreign matter from fluidized furnace |
EP0028458A2 (en) * | 1979-10-03 | 1981-05-13 | Sandfire (Proprietary) Limited | Fluidised-bed boilers |
US4416418A (en) * | 1982-03-05 | 1983-11-22 | Goodstine Stephen L | Fluidized bed residential heating system |
Non-Patent Citations (1)
Title |
---|
PATENTS ABSTRACTS OF JAPAN, Band 4, Nr. 80 (M-15)[562], 10. Juni 1980; & JP - A - 55 41365 (ISHIGAKI KIKOU K.K.) 24.03.1980 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106224947A (en) * | 2016-08-04 | 2016-12-14 | 华北电力大学 | The event-driven control system of Circulating Fluidized Bed Temperature based on feedback of status |
Also Published As
Publication number | Publication date |
---|---|
EP0154690A3 (en) | 1986-03-19 |
DE3407132A1 (en) | 1985-09-05 |
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PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
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AK | Designated contracting states |
Designated state(s): AT BE CH DE FR GB LI LU SE |
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PUAL | Search report despatched |
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17P | Request for examination filed |
Effective date: 19860404 |
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RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: OMNICAL GMBH |
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17Q | First examination report despatched |
Effective date: 19870610 |
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STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
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18D | Application deemed to be withdrawn |
Effective date: 19871020 |
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RIN1 | Information on inventor provided before grant (corrected) |
Inventor name: FREITAG, HANS, DIPL. ING. Inventor name: NOACK, ROLF, DR. DIPL. ING. |