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66 in Firetube Treater, Obround Manway

ASME Section VIII Div. 1, 2023 Edition | Horizontal pressure vessel | 66 in OD SA-516-70 N shell, 14 x 28 in obround firetube manway, two saddles

This worked example documents the ASME Section VIII Division 1 design of a 66 in OD horizontal firetube treater vessel at 110 psig and 450 °F, with a 14 in x 28 in obround firetube manway in the shell. The vessel is SA-516 Grade 70 Normalized at 0.500 in nominal wall, two 2:1 SE heads of the same material, supported on two saddles at 120 ° wrap. MAWP is 185 psig at 450 °F (flange-limited by the Class 150 RFWN process flanges).

The teaching content is the UG-37 area-replacement calculation for the obround firetube manway. The 14 x 28 in opening sits at the 2:1 long-to-short ratio limit of UG-36(c)(2), the upper bound for treating non-round openings under standard UG-37 rules without an Appendix-style special analysis. The area calc is run in both the hoop direction (d = 14 in, F = 1.0) and the longitudinal direction (d = 28 in, F = 0.5). The hoop direction governs and requires a repad; a 0.500 in x 4.000 in plate repad welded full-perimeter around the obround opening provides 4.00 in² of additional reinforcement in the hoop direction, closing the 0.146 in² deficit with 2.4 times the required area.

Code
ASME VIII Div 1, 2023
Design Pressure
110 psig
Design Temperature
450 °F
Design MDMT
-20 °F
Rated MDMT
-45 °F at MAWP
MAWP
185 psig (flange at 450 F)
Shell
66 in OD x 0.500 in, SA-516-70 N
Heads
2:1 SE, 0.500 in SA-516-70 N
Obround Manway
14 x 28 in (2:1), with 0.5 x 4 in repad
Process Flanges
B16.5 Cl 150 RFWN
Empty Weight, New
~7,800 lb
Hydrotest
240 psig (shop)
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Calculation Walkthrough

Five sections. Each section is a collapsible block. Open to read the full design basis, summary tables, materials, code clause index, and the worked numerical examples for this configuration.

1. Design Basis and Code Compliance

Design Conditions

ParameterValueReference
Code of constructionASME Section VIII Division 1, 2023 EditionU-1, U-2
Equipment typeHorizontal firetube treater (indirect-fired vessel with removable U-shaped firetube)
Design pressure110 psigUG-21
Design temperature450 °FUG-20(a)
Design MDMT-20 °FUG-20(b), UCS-66
Corrosion allowance0.0625 in (internal surfaces)UG-25
Joint efficiency, shell1.00 (full RT long seam)UW-12
Joint efficiency, heads1.00 (one-piece formed)UW-12
RadiographyFull RT on Cat. A welds, surface NDE on nozzle welds including the obround manway perimeterUW-11, UW-50
ServiceNon-lethal, non-cyclic. Operating temperature varies with firetube cycling, but the design point envelopes peak operating.UG-22, UW-2

Loadings Considered (UG-22)

The vessel is analyzed for the loadings listed in UG-22. Governing loads for this configuration are:

  • Internal design pressure of 110 psig at 450 °F.
  • Weight of the vessel, the contents (treated oil and water), and the firetube on its support rails.
  • Two-saddle reactions evaluated by the Zick method per Appendix G-1.
  • Thermal gradients at the obround manway during firetube cycling (handled by conservative obround-nozzle wall thickness and the addition of a repad, not by a code-mandatory calc).

The vessel is non-cyclic by UG-22(e) screening despite firetube cycling, because the operating pressure cycles below 50% of design and the thermal gradient zone is bounded by the manway repad. An explicit fatigue check is not required.

Toughness Basis

The Minimum Design Metal Temperature is -20 °F at the full design pressure of 110 psig. The shell and heads are SA-516 Grade 70 Normalized, Curve D under Table UCS-66. Required MDMT at the shell thickness (0.500 in nominal) is approximately -45 °F at no impact testing.

Hydrostatic Test Basis

The shop hydrostatic test follows UG-99(b):

P_test = 1.3 × MAWP × LSR = 1.3 × 185 × 1.00 = 240 psig

SA-516 Grade 70 at 70 °F test temperature has the same allowable stress as at the 450 °F design temperature for ratio purposes; the LSR is 1.00 for the material because the derating from S = 18,800 at 450 °F vs 20,000 at ≤ 300 °F only matters above 300 °F. The flange P-T rating ratio (Cl 150 at 70 °F = 285 psig vs at 450 °F = 185 psig) is favorable for test.

2. Pressure and Thickness Summary

Pressure by Component

ComponentMaterialt_req (in)t_avail (in)MAWP (psig)Clause
Cylindrical shellSA-516 Gr 70 N0.1920.375215UG-27(c)(1)
2:1 ellipsoidal heads (each)SA-516 Gr 70 N0.1910.388223UG-32(d)
14 x 28 in obround firetube manwaySA-105 hub forging, 0.750 in wall on neck, 0.500 x 4 in repadUG-37 PASS with repad0.750matches shellUG-36(c)(2), UG-37 obround
Cl 150 RFWN flanges (process)SA-105standardstandard185UG-44, B16.5 Gp 1.1 at 450 F

The Class 150 process flanges govern the vessel MAWP at 185 psig at 450 °F (between the table values of 200 psig at 400 F and 170 psig at 500 F). Shell and heads are well above the flange rating. The 14 x 28 in obround manway is the design challenge of the page.

Governing Thickness, UG-16(b)

Per UG-16(b), the minimum required thickness is 0.0625 in. All components meet UG-16(b) by a wide margin.

Hydrostatic Test Summary

ComponentCalc Stress at 240 psig (psi)0.9 × S_y at 70 °F (psi)Status
Shell, UG-99 Note 3520,88032,400 (SA-516-70 N)PASS
Heads20,16032,400PASS
Obround manway hub flange (FEA-verified in production)varies, bounded by 18,000 psi peak32,400PASS
3. Materials and Construction

Material Schedule

ComponentSpecificationS at 450 °F (psi)UCS-66 CurveForm
ShellSA-516 Grade 70, normalized18,800D0.500 in plate, rolled and welded long seam
Heads (2 ea)SA-516 Grade 70, normalized18,800D2:1 ellipsoidal, one-piece formed, 0.500 in nominal
Obround manway neckSA-105 hub forging17,500B14 in x 28 in oblong forging, 0.750 in wall on the neck, 2.500 in flange face
Obround manway repadSA-516 Grade 70, normalized18,800D0.500 in x 4.000 in wide, rolled to match the obround perimeter, full-circumference fillet
Process nozzle necksSA-106 Grade B, seamless15,900BNPS 4 / 3 / 2 Sch 80 pipe
Process flangesSA-10517,500BASME B16.5 RFWN Class 150, all process nozzles
SaddlesSA-36 platen/an/a120 ° wrap, 10 in saddle width, two skid-mounted

Nozzle Schedule

TagFunctionSize and ClassLocationTypeWeld
M1Firetube manway (removable U-tube firetube)14 in x 28 in obround, custom SA-105 hub flange with 20 studs on 19 in bolt circle (short dim)Shell, side wall, long axis longitudinalSet-in obround, with 0.500 in x 4.000 in repad full perimeterFull pen + fillet, surface NDE per UW-50 at every quadrant
N1Process inletNPS 4 Cl 150 RFWNTop headSet-in radial, no repad (UG-37 PASS without repad)Full pen + fillet per UW-16(f)
N2Treated-oil outletNPS 3 Cl 150 RFWNBottom head (downstream of weir)Set-in radial, exempt UG-36(c)(3)(a)Full pen + fillet per UW-16(f)
N3Water draw-offNPS 3 Cl 150 RFWNShell, bottom, midspanSet-in radial, exempt UG-36(c)(3)(a)Full pen + fillet per UW-16(f)
N4Gas outlet to stackNPS 4 Cl 150 RFWNShell, top (downstream of weir)Set-in radial, no repadFull pen + fillet per UW-16(f)
N5Pressure relief (PSV)NPS 2 Cl 150 RFWNShell, topSet-in radial, exempt UG-36(c)(3)(a)Full pen + fillet per UW-16(f)

The 14 in x 28 in obround firetube manway is the largest opening on the vessel and is the design challenge of the page. The UG-37 area calc for the obround is in section 5 example 3.

Radiography

Category A welds (long seam and head-to-shell circumferentials) are fully radiographed per UW-11(a)(1). The obround manway perimeter weld is examined by surface NDE at every quadrant per UW-50. Process nozzle welds are surface NDE per UW-50.

Dimensional Summary

ItemValue
Shell OD66.000 in
Shell wall, nominal0.500 in
Shell wall, mill-min (-12.5%)0.438 in
Shell wall, corroded (mill-min less CA)0.375 in
Shell tangent-to-tangent length240 in (20 ft)
Head nominal thickness, 2:1 SE0.500 in
Obround manway, short axis (height)14 in
Obround manway, long axis (length, parallel to vessel axis)28 in
Obround ratio (long / short)2.00 (at the UG-36(c)(2) limit)
Obround manway flange face OD (short direction)19.250 in
Saddle wrap angle120 °
Saddle width10 in
Internal volume, new (shell + 2 heads)~948,000 in³ (4,105 US gal)
Empty weight, new~7,800 lb (incl. obround forging and repad)
Test weight, water-filled~42,600 lb
4. Calculations Performed (Code Clause Index)

Every clause applied, grouped by topic. The obround nozzle calc is the central content of this page.

Wall Thickness

ClauseComponentUse
UG-16(b)AllMinimum 0.0625 in
UG-23AllAllowable stresses at design temperature (SA-516 Gr 70 derates to 18,800 at 450 F)
UG-25AllCorrosion allowance 0.0625 in
UG-27(c)(1)Cylindrical shellInternal pressure, circumferential stress
UG-32(d)2:1 SE headsInternal pressure

Nozzle Reinforcement

ClauseUse
UG-36(c)(2)Permits obround openings with the long-to-short ratio not exceeding 2:1 to be designed under standard UG-37 rules (the obround here is at the 2:1 limit)
UG-36(c)(3)(a)Exempts the NPS 3, NPS 2 process openings from UG-37
UG-37Area replacement procedure, run on the 14 x 28 in obround in worked example 3 and verified on the NPS 4 inlet and gas outlet
UG-41Strength of reinforcement, repad-to-shell weld sized per UG-41
UG-44Cl 150 RFWN flanges at the B16.5 Gp 1.1 P-T rating (185 psig at 450 F)
UG-45Nozzle minimum-thickness check on each neck

Welds

ClauseUse
UW-9 / UW-11(a)(1) / Table UW-12Cat. A and Cat. C weld design, full RT on Cat. A, E = 1.00
UW-15 / UW-16 / UW-50Attachment weld design and NDE; the obround manway perimeter weld receives surface NDE at every quadrant

Supports, Toughness, Test, Marking

ClauseUse
UG-22 / Appendix G-1Loadings and Zick saddle analysis
UCS-66 / UCS-66.1MDMT qualification
UG-99(b) / Note 35Hydrotest at 1.3 × 185 = 240 psig, stress under 0.9 S_y
UG-116 / UG-118 / UG-120(c)Nameplate, location, U-1A data report
5. Worked Examples (Numerical)

Five worked examples. The obround manway UG-37 area calc in example 3 is the central content. Examples 1 and 2 are routine pressure-containment. Example 4 is the NPS 4 inlet check (also UG-37 because of size). Example 5 is the hydrotest summary.

Example 1. Shell Wall Thickness, UG-27(c)(1)

SymbolValueSource
P110 psigDesign pressure
R32.625 inInside radius, corroded: (66 - 2 × 0.375) / 2
S18,800 psiSA-516 Gr 70 at 450 °F, ASME II-D Table 1A
E1.00Full RT long seam, Table UW-12
UG-27(c)(1): t = P R / (S E - 0.6 P) t = 110 × 32.625 / (18,800 - 66) t = 3,589 / 18,734 t = 0.1916 in

Required thickness with CA is 0.254 in. Mill-minimum supplied is 0.438 in (0.500 nominal less 12.5%), corroded to 0.375 in. PASS with 0.121 in margin. Shell MAWP at corroded thickness 0.375 in is 215 psig.

Example 2. 2:1 SE Head Thickness, UG-32(d)

SymbolValueSource
P110 psigDesign pressure
D65.250 inInside diameter at the head skirt (shell ID, corroded)
S18,800 psiSA-516 Gr 70 at 450 °F
E1.00One-piece formed head
K1.002:1 ellipsoidal aspect ratio
UG-32(d): t = P D K / (2 S E - 0.2 P) t = 110 × 65.250 × 1.00 / (37,600 - 22) t = 7,178 / 37,578 t = 0.1910 in

Required thickness with CA is 0.254 in. Head supplied at 0.500 nominal, formed-corroded min 0.388 in. PASS with 0.134 in margin. Head MAWP at 0.388 in formed-corroded is 223 psig.

Example 3. Obround Firetube Manway, UG-36(c)(2) + UG-37

The 14 in x 28 in obround opening in the shell is the design challenge. The obround ratio is 28 / 14 = 2.00, at the upper limit of UG-36(c)(2) for treating obround openings under standard UG-37 rules. Two area calcs are performed: one in the hoop (circumferential) direction using the short axis as `d`, and one in the longitudinal direction using the long axis as `d` with F = 0.5. Both must pass.

SymbolValueSource
d_short (hoop direction)14 inShort axis, perpendicular to vessel axis
d_long (longitudinal direction)28 inLong axis, parallel to vessel axis
t_r0.192 inShell required thickness from Example 1, F = 1.0
t0.375 inShell wall, corroded mill-min
t_n0.750 inObround manway neck wall (custom SA-105 forging)
F (hoop direction)1.00Radial section, full circumferential stress
F (longitudinal direction)0.50Longitudinal section, Fig UG-37 chart at θ = 90 °
f_r10.931S_n / S_v = 17,500 / 18,800 (SA-105 in SA-516-70 N shell at 450 F)

Hoop direction check (d = 14 in, F = 1.0)

A_required = d × t_r × F + 2 × t_n × t_r × F × (1 - f_r1) A_required = 14 × 0.192 × 1.00 + 2 × 0.750 × 0.192 × 1.00 × 0.069 A_required = 2.688 + 0.020 A_required = 2.708 in² Area available in shell (A1): A1a = d × (E1 t - F t_r) = 14 × (0.375 - 0.192) = 2.562 in² A1b = 2 × (t + t_n) × (E1 t - F t_r) = 2 × (0.375 + 0.750) × 0.183 = 0.412 in² A1 = max(A1a, A1b) = 2.562 in²

Hoop-direction A1 = 2.562 in² against A_required = 2.708 in². Shell wall alone is insufficient by 0.146 in². A repad is required.

Longitudinal direction check (d = 28 in, F = 0.5)

A_required = 28 × 0.192 × 0.50 + 2 × 0.750 × 0.192 × 0.50 × 0.069 A_required = 2.688 + 0.010 A_required = 2.698 in² Area available in shell (A1): A1a = 28 × (E1 t - F t_r) = 28 × (0.375 - 0.5 × 0.192) = 28 × 0.279 = 7.812 in² A1 = 7.812 in² (governing path)

Longitudinal-direction A1 = 7.812 in² against A_required = 2.698 in². PASS in the longitudinal direction without repad. The hoop direction governs.

Repad sizing to close the hoop-direction deficit

SymbolValueSource
Repad thickness, t_p0.500 in1/2 in plate, SA-516 Gr 70 N
Repad width per side, w_p4.000 in4 in beyond the opening edge
Repad effective length in hoop direction2 × w_p = 8 in (each side beyond the d_short)
Repad area contribution in the hoop direction (A5): A5 = 2 × w_p × t_p × f_r4 A5 = 2 × 4.000 × 0.500 × 1.00 A5 = 4.00 in²

Total area available with repad in the hoop direction:

A_total = A1 + A5 (+ A2, A3, A4 conservatively neglected) A_total = 2.562 + 4.00 = 6.562 in² vs A_required = 2.708 in²

Margin = 3.854 in², or 142% of A_required. PASS. The 0.500 in x 4 in repad provides 2.4 times the required reinforcement in the hoop direction, with the longitudinal direction already passing without repad. The repad also serves as a thermal-mass buffer at the firetube manway, reducing the through-thickness gradient during firetube cycling.

Example 4. NPS 4 Inlet Nozzle, UG-37

The NPS 4 process inlet on the top head exceeds the UG-36(c)(3)(a) 3.5 in finished-diameter exemption limit. A UG-37 area calc is run.

SymbolValue
d (NPS 4 ID corroded)4.151 in
t_r (head, from example 2)0.191 in
t (head, corroded formed)0.388 in
t_n (NPS 4 Sch 80 wall corroded)0.232 in
F1.00 (radial in 2:1 SE head)
A_required = d × t_r × F = 4.151 × 0.191 × 1.00 = 0.793 in² A1 = d × (E1 t - F t_r) = 4.151 × (0.388 - 0.191) = 0.818 in² A2 (nozzle wall excess, outward) = 2 × h × (t_n - t_rn) ≈ 0.55 in² A_total ≈ 1.37 in² vs A_required 0.793 in²

PASS with 73% margin. No repad required on the NPS 4 inlet.

Example 5. Hydrotest, UG-99(b) Note 35

P_test = 1.3 × MAWP × LSR P_test = 1.3 × 185 × 1.00 = 240 psig
ComponentStress at test (psi)0.9 × S_y at 70 °F (psi)Status
Shell (hoop)240 × 32.625 / 0.375 = 20,88032,400 (SA-516-70 N)PASS
Head (membrane)240 × 65.250 / (2 × 0.388) = 20,18032,400PASS
Obround manway hub flange~17,500 (FEA-bounded in production)32,400PASS

All components carry the test pressure with margin to the 0.9 × S_y limit. The obround manway flange is the highest-stressed component and is verified by FEA in production to bound the local peak below 0.9 S_y; for the code calc the UG-37 area replacement is the controlling rule.

About this example

66 in horizontal firetube treaters are common in upstream oil and gas as heated free-water knockouts and emulsion treaters, where a removable U-shaped firetube provides the heat to break the oil-water emulsion. The teaching value of the example is the UG-37 area-replacement calc applied to the firetube obround manway. Obround openings up to 2:1 long-to-short ratio are permitted under standard UG-37 rules per UG-36(c)(2), with separate hoop-direction and longitudinal-direction checks. The hoop direction governs and a repad is required to close the area deficit; a 0.5 in x 4 in plate repad welded full perimeter is the standard solution.

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Cyclogen5D · Calgary, Canada · ASME Section VIII Div. 1 design, FEA, and CFD for separation and pressure equipment. This page is a generic worked example for educational and reference use. Numerical values illustrate a typical configuration and should not be used as the basis for any built equipment. Project work is sealed under the engineering authority of the project of record.