GB858928A - Method of and apparatus for discharging liquid working medium out of the separator of a forced through-flow steam generator - Google Patents

Method of and apparatus for discharging liquid working medium out of the separator of a forced through-flow steam generator

Info

Publication number
GB858928A
GB858928A GB16095/59A GB1609559A GB858928A GB 858928 A GB858928 A GB 858928A GB 16095/59 A GB16095/59 A GB 16095/59A GB 1609559 A GB1609559 A GB 1609559A GB 858928 A GB858928 A GB 858928A
Authority
GB
United Kingdom
Prior art keywords
line
valve
separator
injection
superheater
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
GB16095/59A
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 GB858928A publication Critical patent/GB858928A/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B29/00Steam boilers of forced-flow type
    • F22B29/06Steam boilers of forced-flow type of once-through type, i.e. built-up from tubes receiving water at one end and delivering superheated steam at the other end of the tubes
    • F22B29/08Steam boilers of forced-flow type of once-through type, i.e. built-up from tubes receiving water at one end and delivering superheated steam at the other end of the tubes operating with fixed point of final state of complete evaporation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B37/00Component parts or details of steam boilers
    • F22B37/02Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
    • F22B37/10Water tubes; Accessories therefor
    • F22B37/101Tubes having fins or ribs
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22GSUPERHEATING OF STEAM
    • F22G5/00Controlling superheat temperature
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22GSUPERHEATING OF STEAM
    • F22G5/00Controlling superheat temperature
    • F22G5/20Controlling superheat temperature by combined controlling procedures

Abstract

858,928. Regulating forced-flow steam boilers. SULZER FRERES S.A. May 11, 1959 [May 22, 1958], No. 16095/59. Classes 123(2) and 123(3) In a method of regulating a forced-flow once-through steam generator, which method remains flexible in spite of the approach of the live steam pressure toward the critical pressure, water, collected in a separator 16 located between a vaporizing section 14 and a superheating section 18, is discharged through an outflow line 19 equipped with a valve 21 which is regulated in accordance with the quantity of liquid present in the separator and is also fed through a line 23 to an injection point 25 in the superheater 18, the amount of injection being controlled by a valve 24 which is incorporated in the line 23 and is controlled by a thermostat 39 heated at the steam-discharge end of the superheater. The discharge valve 21 is controlled by a float 35 acting through a lever 36, a bellcrank lever 37, and a link 38. If desired the thermostat 39 may be located at another point in the superheater such as at the injection point 25 or at a point 42. Steam from the superheater is delivered through a line 26 to a turbine plant 27 which exhausts through a Ine 28 to a condenser 31 from which condensate is urged by a pump 33 through a line 34 to a water vessel 10. A pump 11 feeds water to an economizer 13 connected to the vaporizer 14. In operation, if e.g. the intensity of firing is suddenly increased as a result of a change in load so that the quantity of water separated out in the separator 16 is considerably reduced, the float 35 drops to close the valve 21 accordingly. Fig. 2 shows two-stage injection where additional injection water is branched-off in a line 43 having a valve 44 controlled by a thermastat 46, and in order to meet the greater injection-water requirements an auxiliary supply line 47 is led from the feed line 12. The line 47, containing a valve 48 which is connected to the bellcrank lever 37 by a lever 49 and a link 51 to operate in the opposite sense to the valve 21 so that when the latter is closed the valve 48 opens, joins the line 23 a non-return valve 52 being inserted between the union and the separator 16 to prevent discharge from the line 47 into the separator 16. A valve 53 in the line 47 reduces the pressure in that line to a value slightly above that prevailing in the line 23 thus ensuring, on change over to injection supply from the line 47, that a large pressure rise does not suddenly occur at the injection points while still maintaining sufficient pressure difference to close the non- return valve 52. The valve 53 may be located upstream of the valve 48. Alternative means of reducing an abrupt pressure rise on change over includes a second regulating valve which is disposed in the line 47 downstream of the valve 48 and which is operated by a servomotor which is influenced by the difference in signals received from two pressure sensing devices located respectievly in the line 23 upstream of the non-return valve 52 and downstream of the junction between the lines 23, 47. In a modification, Fig. 5, the valve 48 is by-passed by a line 59 incorporating a valve 61 adjusted in dependence on signals from an instrument 62 which measures the salts concentration of the feedwater in the line 12. If the salt concentration becomes too high then, independent of the float regulation, the injection of water from the separator is discontinued and injection from the feed line 12 is substituted. The instrument 62 could be arranged at another location, e.g. at the separator 16, and the non-return valve 52 could be replaced by valve which is influenced by a salts concentration measuring instrument and is closed on the opening of one of the valves 48, 61. A second vaporizing section may be provided between the separator 16 and the superheater 18 which may be followed by a second separator the outflow of liquid medium to the superheater being from either separator of from both.
GB16095/59A 1958-05-22 1959-05-11 Method of and apparatus for discharging liquid working medium out of the separator of a forced through-flow steam generator Expired GB858928A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CH357413T 1958-05-22

Publications (1)

Publication Number Publication Date
GB858928A true GB858928A (en) 1961-01-18

Family

ID=4511557

Family Applications (1)

Application Number Title Priority Date Filing Date
GB16095/59A Expired GB858928A (en) 1958-05-22 1959-05-11 Method of and apparatus for discharging liquid working medium out of the separator of a forced through-flow steam generator

Country Status (5)

Country Link
BE (1) BE578852A (en)
CH (1) CH357413A (en)
DE (1) DE1127365B (en)
FR (1) FR1224443A (en)
GB (1) GB858928A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2276225A (en) * 1993-03-12 1994-09-21 Westinghouse Electric Corp Temperature control of boiler steam
WO2012062708A3 (en) * 2010-11-10 2013-04-04 Siemens Aktiengesellschaft Fossil fueled steam generator

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH609138A5 (en) * 1976-05-14 1979-02-15 Sulzer Ag Forced-flow steam generator
DE102004062363B4 (en) * 2004-12-13 2010-06-10 Kärcher Futuretech GmbH Apparatus for generating superheated steam and hot water for cleaning or decontamination purposes
DE102009011953B4 (en) * 2009-03-10 2015-06-25 Jumag Dampferzeuger Gmbh Device for removing pressurized hot water from the boiler of a steam generator
DE102016013992A1 (en) * 2016-11-23 2018-05-24 Jumag Dampferzeuger Gmbh SLUDGE CONTAINER WITH LEVEL-CONTROLLED INLET AND OUTLET

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE714895C (en) * 1937-10-02 1941-12-09 Sulzer Ag Arrangement for regulating the operation of a high-pressure, tubular steam generator
DE702231C (en) * 1938-05-08 1941-02-03 Askania Werke Akt Ges Steam temperature controller for forced flow boiler

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2276225A (en) * 1993-03-12 1994-09-21 Westinghouse Electric Corp Temperature control of boiler steam
WO2012062708A3 (en) * 2010-11-10 2013-04-04 Siemens Aktiengesellschaft Fossil fueled steam generator

Also Published As

Publication number Publication date
CH357413A (en) 1961-10-15
BE578852A (en) 1959-11-20
FR1224443A (en) 1960-06-23
DE1127365B (en) 1962-04-12

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