WO1993022599A1 - Zwangdurchlaufdampferzeuger - Google Patents
Zwangdurchlaufdampferzeuger Download PDFInfo
- Publication number
- WO1993022599A1 WO1993022599A1 PCT/DE1993/000344 DE9300344W WO9322599A1 WO 1993022599 A1 WO1993022599 A1 WO 1993022599A1 DE 9300344 W DE9300344 W DE 9300344W WO 9322599 A1 WO9322599 A1 WO 9322599A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- value
- heating surface
- evaporator heating
- steam generator
- setpoint
- Prior art date
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B35/00—Control systems for steam boilers
- F22B35/06—Control systems for steam boilers for steam boilers of forced-flow type
- F22B35/10—Control systems for steam boilers for steam boilers of forced-flow type of once-through type
Definitions
- the invention relates to a once-through steam generator with an evaporator heating surface and with a device connected upstream of the evaporator heating surface to set the feed water mass flow M into the evaporator heating surface and with a control device associated with this device, the controlled variable of which is the feed water mass flow M. and whose setpoint Ms "for the feed water mass flow is guided as a function of a setpoint L assigned to the steam generator output.
- a forced-flow steam generator of the type mentioned at the outset is characterized in accordance with the invention in that the control device is provided with a device for forming the size
- Processing the actual value of the specific enthalpy at the inlet of the evaporator heating surface enables drawing the heat flow flowing into the evaporator heating surface to determine the setpoint for the feed water mass flow, so that the feed water mass flow supplied to the evaporator heating surface can be largely adapted to the heat flow supplied to the evaporator heating surface. This enables targeted guidance of the specific enthalpy at the outlet of the evaporator heating surface.
- Evaporator heating surface measured pressure temporarily reduced by a correction value and temporarily increased by a correction value when this second power value L2 or the actual value of the pressure measured behind the evaporator heating surface decreases.
- Enthalpy is switched at the input of the evaporator heating surface and this temporarily reduces the value of the variable formed as the setpoint Ms g 3 when the actual value h .. - the specific enthalpy at the input of the evaporator heating surface by a correction value and when this actual value h decreases. p temporarily increased by a correction value. This takes into account that the effects of changes in mass flow and temperature of the feed water entering the evaporator heating surface in the evaporator heating surface * are not synchronous.
- Figure 1 shows schematically a once-through steam generator according to the invention.
- FIG. 2 and 3 show in a diagram the time course of the specific enthalpy at the outlet of the evaporator heating surface of the once-through steam generator according to FIG. 1.
- the forced flow steam generator according to Figure 1 has a feed water preheating surface (economizer heating surface) 2, which is located in a gas train, not shown. In terms of flow, this feed water preheating surface 2 is preceded by a feed water pump 3 and an evaporator heating surface 4.
- a measuring device 9 for measuring the actual value h- F of the specific enthalpy of the feed water at the inlet of the evaporator heating surface 4 is provided at the entry of the evaporator heating surface 4 in the connecting line between the feed water preheating heating surface 2 and the evaporator heating surface 4.
- a drive motor on the feed water pump 3 is assigned a very fast controller, specifically a PI controller 6, at the input of which the control deviation ⁇ as a controlled variable.
- the controller 6 is assigned a device 8 for forming the setpoint M for the feed water mass flow.
- This device 8 has, on the one hand, as input variables a setpoint L for the output of the once-through steam generator which is output by a setpoint generator 7 and, on the other hand, the actual value h- F of the specific enthalpy at the inlet of the evaporator heating surface 4 determined by the measuring device 9.
- the setpoint value L of the power of the once-through steam generator which changes time and again during operation and which is fed directly to the fuel controller in the (not shown) firing control loop, is also fed to the input of a first delay element 13 of the device 8.
- This delay element 13 which is of higher order, for example of 2nd order, gives a first signal or a delayed first power worth Ll.
- This first power value L1 is fed to the inputs of function transmitter units 10 and 11 of the function transmitter of the device 8.
- a value M (L1) for the feed water mass flow appears at the output of the function transmitter unit 10, and a value ⁇ h (Ll) for the difference from the specific enthalpy h appears at the output of the function transmitter unit 11.
- the output variables M (L1) and ⁇ h (Ll) of the function generator units 10 and 11 are multiplied together in a multiplication element 14 of the function generator of the device 8.
- the product value Q (L1) obtained corresponds to the heat flow into the evaporator heating surface 4 at the power value Ll.
- This quantity Q (L1) is entered as a counter in a divider 15.
- a setpoint h (L2) is taken from a third function generator unit 12 of the function generator of the device 8.
- the input value of the function generator unit 12 arises at the output of a second delay element 16, in particular a delay element of the first order, the input variable of which is the first power value L1 at the output of the first delay element 13.
- the input value of the third function generator unit 12 is a second power value L2, which is delayed compared to the first power value L1.
- the values h "(L2) as a function of L2 are stored in the third function generator unit 12; they are determined from values for h ", which were respectively obtained during a steady-state operation of the continuous steam generator and were entered into the third function generator unit 12.
- the output of the divider 15 can be the setpoint
- the output of the second delay element 16 there can advantageously be the input of a differentiating element 17, the output of which is switched negatively to a summing element 18.
- This summing element 18 corrects the value for the heat flow Q (L1) into the evaporator heating surface 4 by the output signal of the differentiating element 17.
- the input of the differentiating element 17 can also - as in FIG. 1 only indicated by dashed lines - on a device 30 for measuring the actual value of the pressure p. are located behind the evaporator heating surface 4 (for example also behind a superheater heating surface of the forced-flow steam generator connected downstream in terms of flow).
- Between the input of the differentiating element 17 and such a device 30 for measuring the actual value of the pressure p. can also be connected to a function generator, for example, as the output signal that the measured pressure p. outputs the corresponding saturated steam temperature to the differentiating member 17.
- a further differentiating element 24 can advantageously be provided as a functional element with differentiating behavior.
- This differentiating element 24 has, as an input variable, the actual value h- E of the specific enthalpy at the inlet of the evaporator heating surface 4, determined with the measuring device 9.
- the output of the differentiating element 24 is also connected negatively to the summing element 18.
- the once-through steam generator is in a steady state and the setpoint L for the steam generator output is constant.
- the power values L1 at the output of the delay element 13 and L2 at the output of the delay element 16 are thus also constant; they have the same value as the setpoint L.
- h- E corresponds to the stationary value for the specific enthalpy at the entrance to the evaporator heating surface 4
- the value M output by the device 8 corresponds to the stationary setpoint for the feed water flow into the feed water preheating heating surface 2 and thus into the evaporator heating surface 4.
- ⁇ h (Ll) x M (L1) ⁇ h (L) x M (L) corresponds to a stationary value for the heat flow into the evaporator heating surface 4.
- the differentiator 17 reduces the setpoint value M for the feed water flow by a corresponding correction value as long as the power value L2 increases in time and the heating of the metal masses of the evaporator heating surface 4 reduces the heat flow which is in the mass flow in the evaporator heating surface 4 arrives, reduced.
- the Differentiator 17, on the other hand increases the setpoint M by a corresponding correction value as long as the power value L2 drops in time and the cooling of the metal masses of the evaporator heating surface 4 increases the heat flow that enters the mass flow in the evaporator heating surface 4.
- the output of the differentiating element 17 can also be connected positively to the other summing element 19, possibly via a normalizing element.
- the differentiator 24 reduces the setpoint Ms for the feed water mass flow into the once-through steam generator by a correction value as long as the actual value h- E of the specific enthalpy at the inlet of the
- the differentiator 24 increases the desired value M by a correction value as long as the actual value h- E falls in time.
- the output of the differentiating element 24 can also be connected to the summing element 19 in a positive manner - possibly via a standardization element.
- the differentiating element 24 can be a pure functional element with differentiating behavior. However, it can also include additional computing elements that modify the differentiating behavior.
- the curves I in FIGS. 2 and 3 apply in the event that the output value M (L1) of the function generator unit 10 is the uncorrected setpoint M for the controller 6.
- Curves II apply in the event that differentiators 17 and 24 are not present in the circuit according to FIG. 1, while curves III apply to the circuit corresponding to FIG. 1, but without differentiator 24.
- Curves IV apply to the circuit according to FIG. 1.
- the diagrams according to FIGS. 2 and 3 show that the complete circuit according to FIG. 1 with the curves IV is the cheapest, if there is an overshoot of the specific enthalpy h- A at the outlet of the evaporator heating surface 4 Avoid as much as possible.
- an enthalpy correction controller 20 is also shown in broken lines, the input of which is connected to the output of a summing element 21.
- This summing element 21 is supplied with the desired value h fl (L2) output at the output of the third function transmitter unit 12 and negatively with the actual value h- A of the specific enthalpy at the outlet of the evaporator heating surface 4.
- This actual value h- A is measured with a measuring device 22 located in the outlet line of the evaporator heating surface 4.
- the correction signal at the controller output is fed positively to the summing element 19 of the device 8.
- This enthalpy correction controller 20 advantageously corrects the setpoint Ms "of the feed water flow in the Forced-flow steam generator when the measured actual value h- ft of the specific enthalpy at the outlet of the evaporator heating surface 4 as a result of external interference, such as fluctuations in the calorific value of the fuel supplied to the continuous-flow steam generator or changes in the fire situation in the combustion chamber of the continuous-flow steam generator, from the setpoint h ft (L2) deviates for the specific enthalpy at the outlet of the evaporator heating surface 4, which is emitted by the third function transmitter unit 12.
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE59304751T DE59304751D1 (de) | 1992-05-04 | 1993-04-21 | Zwangdurchlaufdampferzeuger |
EP93908800A EP0639253B1 (de) | 1992-05-04 | 1993-04-21 | Zwangdurchlaufdampferzeuger |
KR1019940703752A KR100251011B1 (ko) | 1992-05-04 | 1993-04-21 | 관류 증기 발생기 |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP92107500 | 1992-05-04 | ||
EP92107500.8 | 1992-05-04 | ||
DEP4217626.3 | 1992-05-27 | ||
DE19924217626 DE4217626A1 (de) | 1992-05-27 | 1992-05-27 | Zwangdurchlaufdampferzeuger |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1993022599A1 true WO1993022599A1 (de) | 1993-11-11 |
Family
ID=25915217
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/DE1993/000344 WO1993022599A1 (de) | 1992-05-04 | 1993-04-21 | Zwangdurchlaufdampferzeuger |
Country Status (8)
Country | Link |
---|---|
US (1) | US5529021A (de) |
EP (1) | EP0639253B1 (de) |
JP (1) | JP2563099B2 (de) |
KR (1) | KR100251011B1 (de) |
CN (1) | CN1044404C (de) |
DE (1) | DE59304751D1 (de) |
DK (1) | DK0639253T3 (de) |
WO (1) | WO1993022599A1 (de) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7624708B2 (en) | 2004-07-09 | 2009-12-01 | Siemens Aktiengesellschaft | Process for operating a continuous steam generator |
EP2194320A1 (de) * | 2008-06-12 | 2010-06-09 | Siemens Aktiengesellschaft | Verfahren zum Betreiben eines Durchlaufdampferzeugers sowie Zwangdurchlaufdampferzeuger |
WO2012110344A1 (de) * | 2011-02-17 | 2012-08-23 | Siemens Aktiengesellschaft | Verfahren zum betrieb eines solarthermischen parabolrinnenkraftwerks |
Families Citing this family (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2152556C1 (ru) * | 1995-03-16 | 2000-07-10 | Сименс АГ | Способ и устройство для контроля подачи питательной воды к парогенератору |
EP2065641A3 (de) | 2007-11-28 | 2010-06-09 | Siemens Aktiengesellschaft | Verfahren zum Betrieben eines Durchlaufdampferzeugers sowie Zwangdurchlaufdampferzeuger |
EP2180250A1 (de) * | 2008-09-09 | 2010-04-28 | Siemens Aktiengesellschaft | Durchlaufdampferzeuger |
EP2182278A1 (de) * | 2008-09-09 | 2010-05-05 | Siemens Aktiengesellschaft | Durchlaufdampferzeuger |
DE102010040210A1 (de) * | 2010-09-03 | 2012-03-08 | Siemens Aktiengesellschaft | Verfahren zum Betreiben eines solarbeheizten Durchlaufdampferzeugers sowie solarthermischer Durchlaufdampferzeuger |
DE102010042458A1 (de) * | 2010-10-14 | 2012-04-19 | Siemens Aktiengesellschaft | Verfahren zum Betreiben einer kombinierten Gas- und Dampfturbinenanlage sowie zur Durchführung des Verfahrens hergerichtete Gas- und Dampfturbinenanlage und entsprechende Regelvorrichtung |
DE102011004263A1 (de) * | 2011-02-17 | 2012-08-23 | Siemens Aktiengesellschaft | Verfahren zum Betreiben eines solarbeheizten Abhitzedampferzeugers sowie solarthermischer Abhitzedampferzeuger |
DE102011004277A1 (de) * | 2011-02-17 | 2012-08-23 | Siemens Aktiengesellschaft | Verfahren zum Betrieb eines direkt beheizten, solarthermischen Dampferzeugers |
EP2655811B1 (de) * | 2011-02-25 | 2015-10-14 | Siemens Aktiengesellschaft | Verfahren zur regelung einer kurzfristigen leistungserhöhung einer dampfturbine |
FR2975797B1 (fr) * | 2011-05-26 | 2020-01-24 | Electricite De France | Systeme de commande pour regulation multivariable de centrale thermique a flamme |
DE102011076968A1 (de) * | 2011-06-06 | 2012-12-06 | Siemens Aktiengesellschaft | Verfahren zum Betreiben eines Umlauf-Abhitzedampferzeugers |
CN109780523B (zh) * | 2016-08-31 | 2020-06-30 | 青岛科技大学 | 一种壁面喷水的智能控制蒸汽干燥机 |
CN109780522B (zh) * | 2016-08-31 | 2020-03-24 | 青岛科技大学 | 一种管束间距控制加热均匀性的蒸汽干燥机 |
CN109780526B (zh) * | 2016-08-31 | 2020-06-23 | 青岛科技大学 | 一种干燥机管箱加热功率的控制方法 |
CN109780525B (zh) * | 2016-08-31 | 2020-06-23 | 青岛科技大学 | 一种干燥机管束管径的控制方法 |
EP3647657A1 (de) * | 2018-10-29 | 2020-05-06 | Siemens Aktiengesellschaft | Speisewasserregelung für zwangdurchlauf-abhitzedampferzeuger |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2133672A1 (de) * | 1971-04-14 | 1972-12-01 | Siemens Ag | |
DE3242968A1 (de) * | 1982-11-20 | 1984-01-12 | Evt Energie- Und Verfahrenstechnik Gmbh, 7000 Stuttgart | Speisewasserregelung und verdampferschutz |
EP0439765A1 (de) * | 1990-01-31 | 1991-08-07 | Siemens Aktiengesellschaft | Dampferzeuger |
-
1993
- 1993-04-21 EP EP93908800A patent/EP0639253B1/de not_active Expired - Lifetime
- 1993-04-21 WO PCT/DE1993/000344 patent/WO1993022599A1/de active IP Right Grant
- 1993-04-21 DE DE59304751T patent/DE59304751D1/de not_active Expired - Lifetime
- 1993-04-21 DK DK93908800.1T patent/DK0639253T3/da active
- 1993-04-21 KR KR1019940703752A patent/KR100251011B1/ko not_active IP Right Cessation
- 1993-04-21 JP JP5518820A patent/JP2563099B2/ja not_active Expired - Lifetime
- 1993-05-04 CN CN93106344A patent/CN1044404C/zh not_active Expired - Lifetime
-
1994
- 1994-11-04 US US08/334,421 patent/US5529021A/en not_active Expired - Lifetime
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2133672A1 (de) * | 1971-04-14 | 1972-12-01 | Siemens Ag | |
DE3242968A1 (de) * | 1982-11-20 | 1984-01-12 | Evt Energie- Und Verfahrenstechnik Gmbh, 7000 Stuttgart | Speisewasserregelung und verdampferschutz |
EP0439765A1 (de) * | 1990-01-31 | 1991-08-07 | Siemens Aktiengesellschaft | Dampferzeuger |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7624708B2 (en) | 2004-07-09 | 2009-12-01 | Siemens Aktiengesellschaft | Process for operating a continuous steam generator |
EP2194320A1 (de) * | 2008-06-12 | 2010-06-09 | Siemens Aktiengesellschaft | Verfahren zum Betreiben eines Durchlaufdampferzeugers sowie Zwangdurchlaufdampferzeuger |
WO2009150055A3 (de) * | 2008-06-12 | 2010-06-17 | Siemens Aktiengesellschaft | Verfahren zum betreiben eines durchlaufdampferzeugers sowie zwangdurchlaufdampferzeuger |
CN102057218A (zh) * | 2008-06-12 | 2011-05-11 | 西门子公司 | 直流式锅炉的运行方法和强制直流式锅炉 |
US9291345B2 (en) | 2008-06-12 | 2016-03-22 | Siemens Aktiengesellschaft | Method for operating a continuous flow steam generator |
WO2012110344A1 (de) * | 2011-02-17 | 2012-08-23 | Siemens Aktiengesellschaft | Verfahren zum betrieb eines solarthermischen parabolrinnenkraftwerks |
Also Published As
Publication number | Publication date |
---|---|
EP0639253B1 (de) | 1996-12-11 |
DE59304751D1 (de) | 1997-01-23 |
CN1044404C (zh) | 1999-07-28 |
KR100251011B1 (ko) | 2000-04-15 |
US5529021A (en) | 1996-06-25 |
EP0639253A1 (de) | 1995-02-22 |
JPH07502803A (ja) | 1995-03-23 |
JP2563099B2 (ja) | 1996-12-11 |
DK0639253T3 (da) | 1997-06-16 |
KR950701420A (ko) | 1995-03-23 |
CN1086299A (zh) | 1994-05-04 |
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