GB894898A - Improvements in vapour generating plant - Google Patents

Improvements in vapour generating plant

Info

Publication number
GB894898A
GB894898A GB5785/61A GB578561A GB894898A GB 894898 A GB894898 A GB 894898A GB 5785/61 A GB5785/61 A GB 5785/61A GB 578561 A GB578561 A GB 578561A GB 894898 A GB894898 A GB 894898A
Authority
GB
United Kingdom
Prior art keywords
steam
boiler
heating gas
pressure vessel
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
GB5785/61A
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.)
Babcock International Ltd
Original Assignee
Babcock and Wilcox Ltd
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 Babcock and Wilcox Ltd filed Critical Babcock and Wilcox Ltd
Publication of GB894898A publication Critical patent/GB894898A/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00Methods of steam generation characterised by form of heating method
    • F22B1/02Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
    • F22B1/023Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers with heating tubes, for nuclear reactors as far as they are not classified, according to a specified heating fluid, in another group
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00Methods of steam generation characterised by form of heating method
    • F22B1/02Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
    • F22B1/18Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
    • F22B1/1823Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines for gas-cooled nuclear reactors

Landscapes

  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Cyclones (AREA)

Abstract

894,898. Vertical steam generators; superheaters. BABCOCK & WILCOX Ltd. Feb. 16, 1961 [Feb. 20, 1960], No. 5785/61. Classes 123(2) and 123(3) In a steam generating unit consisting of an upright cylindrical pressure vessel 1 closed at its ends by domed end caps 2, 3 and containing helicoidal tube banks 19, 20 carrying the heating fluid, for example, the gaseous coolant from a nuclear reactor, the tube banks being disposed in a steam generating space above which is situated an annular steam and water collecting chamber 38 outlets 39 lead from the chamber to a battery of cyclone separators 40 mounted within a drum 33 whence separated steam ascends through driers 42 to a steam space 43 in the upper part of the drum whilst water is discharged by the separators 40 into a pool 41 and returned through an axially disposed downcomer 21 to a liquid inlet chamber 31 for recirculation. Steam leaves the space 43 through secondary drying units 44 and ascends through an annular passage containing a superheater tube nest 10 to leave the vessel 1 through outlets 50. The heating gas enters the pressure vessel 1 through an inlet 4 and is conducted by tubes 8 to the superheater tube bank 10 whence it passes through a pipe 15 and a distributor 17 to the tube banks 19, 20. From the latter the heating gas passes through a collector 24 to an outlet pipe 25 passing through the end cap 3 at the lower end of the pressure vessel. In a modification, Fig. 4, a number of boilers as described above may be arranged in pairs to form two horizontal rows, between which are disposed heating gas supply and collecting mains 70, 71, each boiler 1A being connected to an economiser 60A, wherein the heating gas leaving the boiler is used to heat feedwater flowing to the boiler. In a further modification, Fig. 5, not shown, a separate superheater is used in conjunction with each boiler and economiser unit.
GB5785/61A 1960-02-20 1961-02-16 Improvements in vapour generating plant Expired GB894898A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR894898X 1960-02-20

Publications (1)

Publication Number Publication Date
GB894898A true GB894898A (en) 1962-04-26

Family

ID=9390571

Family Applications (1)

Application Number Title Priority Date Filing Date
GB5785/61A Expired GB894898A (en) 1960-02-20 1961-02-16 Improvements in vapour generating plant

Country Status (1)

Country Link
GB (1) GB894898A (en)

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