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    Page 1of 5Lecture 8 Additional Notes

    Lecture 8: Steam Generators Additional Notes

    Boiler Fittings and Mountings

    An overview of the necessary ttings, accessories and controls for a boiler

    from nameplates and safety valves to gauge glasses and level controls.

    A number of items must be tted to steam boilers, all with the obective of

    improving operation, e!ciency and safety.

    Boiler name-plate

    "n the latter half of the #$th century e%plosions of

    steam boilers were commonplace. As a conse&uence of

    this, a company was formed in 'anchester with the

    obective of reducing the number of e%plosions by

    subecting steam boilers to independent e%amination.

    After a comparatively short period, only eight out of the

    ## ((( boilers e%amined e%ploded. )his compared to

    *+( steam boiler e%plosions in boilers not e%amined by the scheme. )his

    success led to the oiler -%plosions Act #88*/ which included a re&uirement

    for a boiler name0plate.

    Safet !al!es

    An important boiler tting is the safety valve. "ts function is to

    protect the boiler shell from over pressure and subse&uent

    e%plosion. 'any di1erent types of safety valves are tted to

    steam boiler plant, but generally they must all meet the following

    criteria2

    )he ma%imum set pressure of the safety valve shall be the design or

    ma%imum permissible wor3ing pressure/ of the

    boiler.

    )here must be an ade&uate margin between the normal operating

    pressure of the boiler and the set pressure of the safety valve.

    )he discharge pipewor3 from the safety valve must be unobstructed and

    drained at the base to prevent the accumulation of condensate. "t is good

    practice to ensure that the discharge pipewor3 is 3ept as short as possible

    with the minimum number of bends, so that the allowable bac3pressure

    Fig" 8"# Boiler

    Fig" 8"$ Boiler

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    Page %of 5Lecture 8 Additional Notes

    indicated by the valve manufacturer is not e%ceeded. "t will be &uite normal

    for the internal diameter of the discharge pipewor3 to be more than the

    internal diameter of the safety valve outlet connection, but under no

    circumstances should it be less.

    Boiler stop !al!es

    A steam boiler must be tted with a stop valve also 3nown

    as a crown valve/ which isolates the steam boiler and its

    pressure from the process or plant. "t is generally an angle

    pattern globe valve of the screw0down variety. 4igure 5.6.5

    shows a typical stop valve of this type. 'any boilerma3ers

    use 7 spheroidal graphite/ iron valves as standard.

    )he stop valve is not designed as a throttling valve, and should be fully open

    or closed. "t should always be opened slowly to prevent any sudden rise in

    downstream pressure and associated waterhammer, and to help restrict thefall in boiler pressure and any possible associated priming.

    Feed&ater c'ec( !al!es

    )he feedwater chec3 valve as shown in 4igures 5.6.9

    and 5.6.:/ is installed in the boiler feedwater line

    between the feedpump and boiler. A boiler feed stop

    valve is tted at the boiler shell.

    )he chec3 valve includes a spring e&uivalent to thehead of water in the elevated feedtan3 when there is no

    pressure in the boiler. )his prevents the boiler being

    ;ooded by the static head from the boiler feedtan3.

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    ,S control

    )his controls the amount of )otal >issolved 7olids

    )>7/ in the boiler water, and is sometimes also

    referred to as ?continuous blowdown?. )he )>7 in a

    sample of boiler water is compared with a set point@ if the )>7 level is too high, a &uantity of boiler water is

    released to be replaced by feedwater with a much

    lower )>7 level. )his has the e1ect of diluting the

    water in the boiler, and reducing the )>7 level. n a

    manually controlled )>7 system, the boiler water

    would be sampled every shift.

    A typical automatic )>7 control system is shown in

    4igure 8.8

    .ressure gauge

    All boilers must be tted with at least one pressure

    indicator. "t should be mar3ed to indicate the normal

    wor3ing pressure and the ma%imum permissible wor3ing pressure B design

    pressure. Pressure gauges are connected to the steam space of the boiler and

    usually have a ring type siphon tube which lls with

    condensed steam and protects the dial mechanism

    from high temperatures.

    Pressure gauges may be tted to other pressure containers such as

    blowdown vessels, and will usually have smaller dials as shown in 4igure5.6.$.

    Gauge glasses and /ttings

    All steam boilers are tted with at least one water

    level indicator, but those with a rating of #(( 3= or

    more should be tted with two indicators. A gauge

    glass shows the current level of water in the boiler,

    regardless of the boiler?s operating conditions.

    auge glasses should be installed so that their

    lowest reading will show the water level at :( mm above the point whereoverheating will occur. )hey should also be tted with a protector around

    them, but this should not hinder visibility of the water level. 4igure 8.#(

    shows a typical gauge glass.

    auge glasses are prone to damage from a number of sources, such as

    Fig" 8"8 ,pical

    automatic ,S

    Fig" 8"0 ,pical

    pressure gauge

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    Page $of 5Lecture 8 Additional Notes

    corrosion from the chemicals in boiler water, and erosion during blowdown,

    particularly at the steam end.

    ater le!el controls

    )he maintenance of the correct water level in a steam boiler is essential to its

    safe and e!cient operation. )he methods of

    sensing the water level, and the subse&uent

    control of water level is a comple% topic that is covered by a number of

    regulations.

    23ternal le!el control c'am4er

    )he function of the level controls or alarms is chec3ed daily using the

    se&uencing purge valves.

    Fig" #"+"1#

    nternall mounted le!el controls

    Air vents and vacuum brea3ers

    =hen a boiler is started from cold, the steam space is full of air. )his air has

    no heat value, and will adversely a1ect steam plant performance due to its

    e1ect of blan3eting heat e%change surfaces. )he air can also give rise to

    corrosion in the condensate system, if not removed ade&uately.

    )he air may be purged from the steam space using a simple coc3@ normally

    this would be left open until a pressure of about (.: bar is showing on the

    pressure gauge. An alternative to the coc3 is a balanced pressure air vent

    which not only relieves the boiler operator of the tas3 of manually purging air

    Fig" 8"16 Gauge glass

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    Page 5of 5Lecture 8 Additional Notes

    and hence ensures that it is actually done/, it is also much more accurate

    and will vent gases which may accumulate in the boiler. )ypical air vents are

    shown in 4igure 5.6.#9.

    =hen a boiler is ta3en o10line, the steam in the steam space condenses and

    leaves a vacuum. )his vacuum causes pressure to be e%erted on the boilerfrom the outside, and can result in boiler inspection doors lea3ing, damage to

    the boiler ;at plates and the danger of overlling a shutdown boiler. )o avoid

    this, a vacuum brea3er see 4igure 5.6.#9/ is re&uired on the boiler shell.

    Fig" #"+"1$

    ,pical air !ents and !acuum 4rea(ers