Section 11 Furnaces subject to external pressure
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Clasifications Register Rules and Regulations - Rules and Regulations for the Classification of Ships, July 2022 - Part 5 Main and Auxiliary Machinery - Chapter 10 Steam Raising Plant and Associated Pressure Vessels - Section 11 Furnaces subject to external pressure

Section 11 Furnaces subject to external pressure

11.1 Maximum thickness

11.1.1 Furnaces, plain or corrugated, are not to exceed 22,5 mm in thickness.

11.2 Corrugated furnaces

11.2.1 The minimum thickness, t, of corrugated furnaces is to be determined by the following formula:

= where p and c are as defined in Pt 5, Ch 10, 1.2 Definition of symbols
t = thickness of the furnace plate measured at the bottom of the corrugations, in mm
C = 1060 for Fox, Morison and Deighton corrugations
= 1130 for Suspension Bulb corrugations
D o = external diameter of the furnace measured at the bottom of the corrugations, in mm.

11.3 Plain furnaces, flue sections and combustion chamber bottoms

11.3.1 The minimum thickness, t, between points of substantial support, of plain furnaces or furnaces strengthened by stiffening rings, of flue sections and of the cylindrical bottoms of combustion chambers is to be determined by the following formulae the greater of the two thicknesses obtained being taken:

= where t, c and p are as defined in Pt 5, Ch 10, 1.2 Definition of symbols
C = or 0,85 whichever is the greater
D o = external diameter of the furnace, flue or combustion chamber, in mm
L = length of section between the centres of points of substantial support, in mm

x and σ are as defined in Pt 5, Ch 10, 11.7 Dished and flanged ends for unsupported vertical boiler furnaces 11.7.1.

11.3.2 Where stiffeners are used for strengthening plain cylindrical furnaces, or combustion chambers, the second moment of area, I, of the stiffener is to be determined by the following formula:

where p is as defined in Pt 5, Ch 10, 1.2 Definition of symbols

D o = external diameter of the furnace flue or combustion chamber, in mm
L = length of section between the centres of points of substantial support, in mm

For proportion of stiffening rings, see Figure 10.11.1 Furnace, flue and combustion chamber stiffeners.

11.4 Plain furnaces of vertical boilers

11.4.1 The thickness of plain furnaces not exceeding 2000 mm in external diameter is to be determined by the formulae given in Pt 5, Ch 10, 11.3 Plain furnaces, flue sections and combustion chamber bottoms 11.3.1, the greater of the two thicknesses being taken:

where
D o = external diameter of the furnace, in mm. Where the furnace is tapered, the diameter to be taken for calculation purposes is to be the mean of that at the top and that at the bottom where it meets the substantial support from flange, ring or row of stays
L = effective length, in mm, of the furnace between the points of substantial support as indicated in Figure 10.11.2 Effective length, L, for use in 11.4 .

Figure 10.11.1 Furnace, flue and combustion chamber stiffeners

11.4.2 For furnaces under 760 mm in external diameter, the thickness is to be not less than 8 mm, and for furnaces 760 mm in external diameter and over, the thickness is to be not less than 9,5 mm.

11.4.3 A circumferential row of stays connecting the furnace to the shell will be considered to provide substantial support to the furnace, provided that:

  • The diameter of the stay is not less 22,5 mm or twice the thickness of the furnace, whichever is the greater.
  • The pitch of the stays at the furnace does not exceed 14 times the thickness of the furnace.

11.5 Hemispherical furnaces

11.5.1 The minimum thickness, t, of unsupported hemispherical furnaces subject to pressure on the convex surface is to be determined by the following formula:

= where t, c and p are as defined in Pt 5, Ch 10, 1.2 Definition of symbols
= x and σ are as defined in Pt 5, Ch 10, 11.7 Dished and flanged ends for unsupported vertical boiler furnaces 11.7.1
C = or 0,85 whichever is greater
R o = outer radius of curvature of the furnace, in mm.

11.5.2 In no case is the maximum thickness to exceed 22,5 mm or the ratio to exceed 100.

Figure 10.11.2 Effective length, L, for use in 11.4

11.6 Dished and flanged ends for supported vertical boiler furnaces

11.6.1 The minimum thickness, t, of dished and flanged ends for vertical boiler furnaces that are subject to pressure on the convex side and are supported by central uptakes, is to be determined by the following formula:

where t, p, Ro, c and σ are as defined in Pt 5, Ch 10, 1.2 Definition of symbols.

11.6.2 The inside radius of dishing and flanging are to be as required by Pt 5, Ch 10, 10.3 Dished and flanged ends for vertical boilers.

11.7 Dished and flanged ends for unsupported vertical boiler furnaces

11.7.1 The minimum thickness, t, of dished and flanged ends for vertical boiler furnaces that are subject to pressure on the convex side and are without support from stays of any kind, is to be determined by the following formula, but is in no case to be less than the thickness of the firebox:

where t, c and p are as defined in Pt 5, Ch 10, 1.2 Definition of symbols.

x = specified minimum lower yield stress or 0,2 per cent proof stress in N/mm2 at a temperature 90°C above the saturated steam temperature corresponding to the design pressure for carbon and carbon manganese steel with a specified minimum tensile strength of 400 N/mm2
C = or 0,85 whichever is the greater
R o = outside radius of the crown plate, in mm
= (in no case is to exceed 88)
σ = specified minimum lower yield stress or 0,2 per cent proof stress in N/mm2 at a temperature 90°C above the saturated steam temperature corresponding to the design pressure for the steel actually used

11.7.2 The inside radius of curvature, R i, of the end plate is to be not greater than the external diameter of the cylinder to which it is attached.

11.7.3 The inside knuckle radius, r i, see Figure 10.4.2 Typical dished ends(a), of the arc joining the cylindrical flange to the spherical surface of the end is to be not less than four times the thickness of the end plate and in no case less than 65 mm.

11.8 Ogee rings

11.8.1 The minimum thickness, t, of the ogee ring which connects the bottom of the furnace to the shell of a vertical boiler and sustains the whole vertical load on the furnace is to be determined by the following formula:

= where t, c and p are as defined in Pt 5, Ch 10, 1.2 Definition of symbols
D i = inside diameter of boiler shell, in mm
D o = outside diameter of the lower part of the furnace where it joins the ogee ring, in mm.

11.8.2 Proposals to use a flat plate annular ring which connects the bottom of the furnace to the shell of a vertical boiler and sustains any unbalanced vertical load on the furnace will be the subject of special consideration.

11.9 Uptakes of vertical boilers

11.9.1 The minimum thickness, t, of internal uptakes of vertical boilers is to be determined by the following formulae, the greater of the two thicknesses obtained being taken:

= where t and p are as defined in Pt 5, Ch 10, 1.2 Definition of symbols
D o = external diameter of uptake, in mm
L = length of uptake between the centres of points of substantial support, in mm.

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