GB1338068A - Steam power plant - Google Patents

Steam power plant

Info

Publication number
GB1338068A
GB1338068A GB235171A GB235171A GB1338068A GB 1338068 A GB1338068 A GB 1338068A GB 235171 A GB235171 A GB 235171A GB 235171 A GB235171 A GB 235171A GB 1338068 A GB1338068 A GB 1338068A
Authority
GB
United Kingdom
Prior art keywords
steam
valve
feedwater
separator
flow
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
Application number
GB235171A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sulzer AG
Original Assignee
Sulzer AG
Gebrueder Sulzer AG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sulzer AG, Gebrueder Sulzer AG filed Critical Sulzer AG
Publication of GB1338068A publication Critical patent/GB1338068A/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B35/00Control systems for steam boilers
    • F22B35/06Control systems for steam boilers for steam boilers of forced-flow type
    • F22B35/10Control systems for steam boilers for steam boilers of forced-flow type of once-through type
    • F22B35/105Control systems for steam boilers for steam boilers of forced-flow type of once-through type operating at sliding pressure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22GSUPERHEATING OF STEAM
    • F22G5/00Controlling superheat temperature
    • F22G5/20Controlling superheat temperature by combined controlling procedures

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

1338068 Steam generators SULZER BROS Ltd 18 Jan 1971 [19 Jan 1970] 2351/71 Heading F4A In a steam plant, heat is extracted from steam produced in the evaporator 8 to heat the feedwater, and upon occurrence of a peak load, the rate of heat extraction is temporarily reduced. A forced circulation plant has a feedwater vessel 1 from which the water is drawn by pump 2 and delivered through valve 48 to an economizer 3 leading to a mixing vessel 27 in parallel with a separator 39. The water is drawn through line 25 by circulation pump 26 and forced through the evaporator 8 heated by a burner 42. Steam passes through three-way valve 21<SP>1</SP> into the separator 39 and then through two-stage superheater 10 into live steam line 11 which feeds a turbine 12. Thic comprises two stages with an intermediate reheater 31. Exhaust steam from the turbine is condensed at 13 and delivered by pump 14 into the vessel 1. During normal operation some steam is fed from valve 21<SP>1</SP> through pipe 40 into the mixer 27 to heat the feedwater. Valve 21<SP>1</SP> is operated by an actuator 37 controlled by means 36 responsive to the live steam pressure measured by detector 33, or alternatively to the rate of flow. When peak load occurs the pressure falls and valve 21<SP>1</SP> reduces the steam supply to the mixer 27. Simultaneously the pressure detector 33 acts on controller 34 and load controller 35 to open valve 44 and increase the fuel supply to burner 42. The three-way valve 21<SP>1</SP>is also influenced by the flow of water to an injection line 29 which controls the degree of superheat. This flow is controlled by a valve 30 responsive to the live steam temperature. The flow of feedwater to the economizer 3 is controlled by the level in the separator 39 acting upon a sensor 46 which controls the ! valve 48. In another embodiment, Fig. 3 (not shown), the separator and mixer form a single unit (39) and the three-way valve (21<SP>11</SP>) is disposed between this separator and the economizer 3. This valve (21<SP>11</SP>) controls the quantity of feedwater sprayed into the separator and is itself controlled by the output of an electric generator (61) driven by the turbine. In a further embodiment, Fig. 1 (not shown), applied to a natural circulation steam plant, the three-way valve (21) is disposed between the economizer 3 and a steam/water drum (5, and controls the quantity of feedwater sprayed into the drum. The three-way valve is itself controlled in dependence upon the water level in the drum, the actual flow rate of feedwater and the flow rate of steam on the live steam line. The fuel supply is also increased at peak load.
GB235171A 1970-01-19 1971-01-18 Steam power plant Expired GB1338068A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CH67670A CH519098A (en) 1970-01-19 1970-01-19 Method for operating a steam power plant and plant for performing the method

Publications (1)

Publication Number Publication Date
GB1338068A true GB1338068A (en) 1973-11-21

Family

ID=4192557

Family Applications (1)

Application Number Title Priority Date Filing Date
GB235171A Expired GB1338068A (en) 1970-01-19 1971-01-18 Steam power plant

Country Status (9)

Country Link
US (1) US3742709A (en)
BE (1) BE761695A (en)
CA (1) CA919043A (en)
CH (1) CH519098A (en)
DE (1) DE2006410B2 (en)
ES (1) ES387254A1 (en)
FR (1) FR2075725A5 (en)
GB (1) GB1338068A (en)
SE (1) SE362114B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH642155A5 (en) * 1979-08-22 1984-03-30 Sulzer Ag STEAM GENERATOR WITH PARTITION BETWEEN TWO COMBUSTION CHAMBERS.
CN1038611C (en) * 1992-11-30 1998-06-03 四川电力科学试验研究所 Alternative water-supply temp.-reducing method system
US8337139B2 (en) * 2009-11-10 2012-12-25 General Electric Company Method and system for reducing the impact on the performance of a turbomachine operating an extraction system

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2550683A (en) * 1946-08-17 1951-05-01 Babcock & Wilcox Co Attemperator
US2526898A (en) * 1947-06-17 1950-10-24 Bailey Meter Co Vapor temperature control
DE1074169B (en) * 1956-10-31 1960-01-28 General Electric Company, Schenectady (V. St. A.) Control system for a boiling water reactor with double circuit
US3338053A (en) * 1963-05-20 1967-08-29 Foster Wheeler Corp Once-through vapor generator start-up system
US3411299A (en) * 1967-01-25 1968-11-19 Nettel Frederick Peak load operation in steam power plants

Also Published As

Publication number Publication date
US3742709A (en) 1973-07-03
CA919043A (en) 1973-01-16
CH519098A (en) 1972-02-15
DE2006410A1 (en) 1971-07-29
DE2006410B2 (en) 1972-03-30
ES387254A1 (en) 1973-05-01
BE761695A (en) 1971-07-19
FR2075725A5 (en) 1971-10-08
SE362114B (en) 1973-11-26

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PLNP Patent lapsed through nonpayment of renewal fees