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24 in Vertical Vessel with Hub-Flange End Closure

ASME Section VIII Div. 1, 2023 Edition | Vertical pressure vessel | 24 in OD SA-516-70 N, top 2:1 SE head + bottom Appendix 2 hub-flange end closure with bolted blind cover

This worked example documents the ASME Section VIII Division 1 design of a 24 in OD vertical pressure vessel at 285 psig and 300 °F where one end (the bottom) is closed by a bolted Appendix 2 hub-flange and blind cover (quick-opening configuration, typical for filter housings and batch reactors that require periodic element or bundle removal). The top is a welded 2:1 SE head. The vessel is SA-516 Grade 70 Normalized throughout, with a custom hub-flange forging at the bottom (4 in flange thickness, 2.75 in hub-neck thickness as revised). MAWP is 285 psig at 300 °F (design = MAWP).

This page differs from #15 (60 in vessel with a side manway) by applying Appendix 2 to the VESSEL END closure where the flange diameter equals the vessel diameter and the hub structural stresses (S_H, S_R, S_T) become the controlling check, not the bolt area. Worked example 3 walks the full Appendix 2 calc with two iterations: initial g_1 = 2.500 in hub neck FAILS on the (S_H + S_T) / 2 combined-stress check by 2%, revised g_1 = 2.750 in PASSES with 7% margin. The other worked examples cover the shell, the top head, the bolted blind cover (with the UG-34(c)(1) Sketch (m) lever-arm correction), and the UG-37 area check at the hub-to-shell penetration.

Code
ASME VIII Div 1, 2023
Design Pressure
285 psig
Design Temperature
300 °F
Design MDMT
-20 °F
Rated MDMT
-20 °F at MAWP
MAWP
285 psig
Shell
24 in OD x 0.625 in, SA-516-70 N
Top Head
2:1 SE, 0.500 in SA-516-70 N (welded)
Bottom Closure
Appendix 2 hub flange + bolted blind
Closure Bolts
32 x 1-1/4 in B7 on 28 in BC
Closure Cover
2.250 in SA-516-70 N
Hydrotest
562 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 typeVertical pressure vessel with bolted hub-flange end closure (quick-opening filter housing or batch reactor)
Design pressure285 psigUG-21
Design temperature300 °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, top head1.00 (one-piece formed)UW-12
RadiographyFull RT on Cat. A welds, surface NDE on the hub-flange to shell weldUW-11, UW-50
ServiceNon-lethal, non-cyclic, batch process or filter service requiring periodic bundle / element accessUG-22, UW-2

Loadings Considered (UG-22)

Internal design pressure of 285 psig at 300 °F is the governing pressure load. The hub-flange closure sees the bolt-up gasket-seating load plus the operating pressure load, both calculated to Appendix 2 in section 5. Support is by two welded support lugs on the upper shell. Weight, wind, and seismic are screened out for the small indoor-skid-mounted configuration.

Toughness Basis

The design MDMT is -20 °F. Shell, top head, and bottom hub flange are SA-516 Grade 70 Normalized, Curve D under Table UCS-66 (the hub flange is forged from heavy plate). Required MDMT at 0.625 in shell is approximately -45 °F; at the 4.000 in hub-flange thickness, required MDMT is approximately +20 °F without UCS-66.1 credit. With the UCS-66.1 stress-ratio reduction (calc shows ratio < 0.35), the credit covers the gap and rates the hub flange to -20 °F.

Hydrostatic Test Basis

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

P_test = 1.3 × MAWP × LSR = 1.3 × 432 × 1.00 = 562 psig

SA-516 Grade 70 derates slightly at 300 °F (S = 19,500 vs 20,000 at 200 °F) but does not derate below 300 °F at the 70 °F test temperature; LSR = 1.00.

2. Pressure and Thickness Summary

Pressure by Component

ComponentMaterialt_req (in)t_avail (in)MAWP (psig)Clause
Cylindrical shellSA-516 Gr 70 N0.3310.484432UG-27(c)(1)
Top 2:1 SE head, 0.500 in nominalSA-516 Gr 70 N0.3310.388312UG-32(d)
Bottom hub-flange end closure (Appendix 2 custom)SA-105 / SA-516 Gr 70 N hubsee Ex. 34.000 in flange thickness285Appendix 2
Bottom bolted blind coverSA-516 Gr 70 N platesee Ex. 42.250 in285UG-34(c)(1) Sketch (m)
Process nozzles, Cl 300 RFWN flangesSA-105standardstandard655UG-44, B16.5 Gp 1.1 at 300 F

The 2:1 SE head governs the vessel MAWP at 312 psig at 300 F (head thickness slightly tight). For a published rating of 285 psig (design = MAWP), the head is adequate; if a margin above design were required, increase head nominal to 0.625 in. The bolted hub-flange end closure is sized to match the vessel MAWP.

Governing Thickness, UG-16(b)

All components meet UG-16(b).

Hydrostatic Test Summary

ComponentCalc Stress at 562 psig (psi)0.9 × S_y at 70 °F (psi)Status
Shell, UG-99 Note 3513,61032,400PASS
Top SE head14,16532,400PASS
Hub-flange S_H at test~21,000 (FEA-checked in production)32,400PASS
Bolted blind cover~25,000 at test pressure32,400PASS
3. Materials and Construction

Material Schedule

ComponentSpecificationS at 300 °F (psi)UCS-66 CurveForm
ShellSA-516 Grade 70, normalized19,500D24 in OD x 0.625 in plate x 36 in tan-tan
Top head (2:1 SE)SA-516 Grade 70, normalized19,500D2:1 ellipsoidal, one-piece formed, 0.500 in nominal
Bottom hub-flange end closureSA-105 hub forging with integral SA-516 Gr 70 N flange face17,500 / 19,500B / DNPS 24 hub-flange forging, 4.00 in flange thickness, hub OD matched to shell OD, neck 2.50 in thick
Bottom bolted blind coverSA-516 Grade 70 N plate19,500D2.250 in plate, 32 in OD, bolt circle 28 in
Closure gasketSpiral-wound, 304 SS inner + outer ring, flexible-graphite fillern/an/am = 3.0, y = 10,000 psi (Table 2-5.1)
Closure boltingSA-193 Gr B7 studs, SA-194 Gr 2H nuts25,000n/a32 studs, 1-1/4 in UNC, stress area 0.969 in² per stud
Process nozzles + flangesSA-106 Gr B / SA-10516,500 / 17,500BNPS 4 inlet, NPS 4 outlet, NPS 2 PSV, NPS 1 instrument tap, all Cl 300 RFWN

Nozzle Schedule

TagFunctionSize and ClassLocationType
C1Bottom hub-flange end closure (filter element / batch access)NPS 24 Cl 600 custom hub flange, 32 studs of 1-1/4 in UNC on 28 in BC, 4 in flange thicknessBottom of vessel, replaces a welded headIntegral hub forging welded to the shell bottom course, full pen + fillet, surface NDE per UW-50
N1Process inletNPS 4 Cl 300 RFWNTop headSet-in radial, no repad (UG-37 PASS)
N2Process outletNPS 4 Cl 300 RFWNShell, lower (above the hub flange)Set-in radial, no repad
N3Pressure relief (PSV)NPS 2 Cl 300 RFWNTop headSet-in radial, exempt UG-36(c)(3)(a)
N4Instrument tapNPS 1 Cl 300 RFWNShellSet-in radial, exempt UG-36(c)(3)(a)

Radiography

Cat. A welds (shell long seam, top head-to-shell circumferential) fully radiographed per UW-11(a)(1). The hub-flange-to-shell circumferential weld (bottom) is full-penetration with surface NDE at every quadrant per UW-50; it is a Cat. A weld and carries the full vessel pressure load.

Dimensional Summary

ItemValue
Shell OD24.000 in
Shell wall, nominal0.625 in
Shell wall, corroded (mill-min less CA)0.484 in
Shell tangent-to-tangent length36 in (3 ft)
Top head nominal thickness, 2:1 SE0.500 in
Top head minimum corroded0.388 in
Bottom hub flange thickness4.000 in
Bottom hub neck (axial extension below shell bottom)6.000 in long, 2.50 in thick
Bottom blind cover thickness2.250 in
Bottom flange OD x BC32 in x 28 in
Closure bolts32 studs, 1-1/4 in UNC, SA-193 Gr B7
Internal volume, new~17,800 in³ (77 US gal)
Empty weight, new (incl. hub flange and bolting)~2,950 lb (hub flange forging is the heaviest single piece)
Test weight, water-filled~3,600 lb
4. Calculations Performed (Code Clause Index)

Every clause applied. The Appendix 2 hub-flange calc with hub stresses (S_H, S_R, S_T) is the central content.

Appendix 2 Flange Design

ClauseUse
Appendix 2-3Flange design loads: H, H_T, H_G, H_D, with both seating and operating conditions
Appendix 2-4Bolt sizing W_m1, W_m2, A_m
Appendix 2-5Flange stresses S_H (hub longitudinal), S_R (radial), S_T (tangential)
Appendix 2-7Hub-and-flange geometry factors (F, V, e, d, K, U, Y, T, Z, h_0, h_D, h_G, h_T)
Table 2-5.1 (ASME II-D)Gasket factors m and y for spiral-wound flexible-graphite

Wall Thickness

ClauseComponentUse
UG-16(b)AllMinimum 0.0625 in
UG-23AllAllowable stresses at design T
UG-25AllCorrosion allowance
UG-27(c)(1)Cylindrical shell, nozzle necksInternal pressure, circumferential stress
UG-32(d)Top 2:1 SE headInternal pressure
UG-34(c)(1) Sketch (m)Bottom bolted blind coverFlat bolted cover with gasket inside bolt circle, lever-arm correction term

Nozzle Reinforcement and Standard Fittings

ClauseUse
UG-36(c)(3)(a)Exempts NPS 2 PSV and NPS 1 instrument; NPS 4 process nozzles require UG-37
UG-37Area replacement on NPS 4 inlet/outlet and on the NPS 24 hub-flange-to-shell penetration
UG-41Strength of reinforcement (the hub neck serves as the nozzle wall reinforcement at the bottom end closure)
UG-44Cl 300 RFWN process flanges at the B16.5 P-T rating

Welds, Toughness, Test, Marking

ClauseUse
UW-9 / UW-11(a)(1) / Table UW-12Cat. A welds (long seam and head circumferentials, hub circumferential), full RT, E = 1.00
UW-15 / UW-16 / UW-50Nozzle welds and NDE; hub-to-shell weld is surface NDE at every quadrant
UCS-66 / UCS-66.1MDMT qualification; hub flange (4.000 in thick) uses UCS-66.1 stress credit to cover the gap from no-credit MDMT +20 F to the design -20 F
UG-99(b) / Note 35Hydrotest at 562 psig
UG-116 / UG-118 / UG-120(c)Nameplate, location, U-1A
5. Worked Examples (Numerical)

Five worked examples. The Appendix 2 hub-flange design with hub-stress S_H (example 3) is the central content; it differs from a manway-type Appendix 2 application by being a much larger flange (vessel-diameter) where the hub structural stress dominates rather than the bolting.

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

SymbolValue
P285 psig
R11.516 in (inside radius, corroded)
S19,500 psi (SA-516 Gr 70 at 300 F, slight derate)
E1.00
UG-27(c)(1): t = P R / (S E - 0.6 P) = 285 × 11.516 / (19,500 - 171) t = 3,282 / 19,329 = 0.1698 in

Required thickness with CA is 0.232 in. t_avail 0.484 in. PASS with 0.252 in margin. Shell MAWP 432 psig.

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

UG-32(d): t = P D K / (2 S E - 0.2 P) = 285 × 22.969 × 1.00 / (39,000 - 57) t = 6,546 / 38,943 = 0.1681 in

Required thickness with CA is 0.230 in. Head t_avail 0.388 in (formed-corroded). PASS with 0.158 in margin. Head MAWP 312 psig.

Example 3. Bottom Hub-Flange End Closure, Appendix 2

The bottom end of the vessel is closed by a custom Appendix 2 hub-flange (rather than a welded head). The flange face mates against a bolted blind cover with a spiral-wound gasket. The hub neck welds into the bottom course of the shell and extends 6 in below the shell tangent. The full Appendix 2 calc is run to size the flange thickness, bolt count, and verify the hub structural stresses.

Geometry and material inputs

SymbolValue
B (inside diameter of flange)22.875 in
A (flange OD)32.000 in
C (bolt circle)28.000 in
G (gasket reaction diameter, spiral-wound)24.500 in
g_0 (hub thickness at small end, at the shell)0.625 in (matches shell t)
g_1 (hub thickness at large end, at the back of the flange)2.500 in
h (hub length)6.000 in
t (flange thickness)4.000 in
m (gasket factor)3.00
y (gasket seating stress)10,000 psi
S_f (flange allowable, SA-105 at 300 F)17,500 psi

Bolt loads

H = (π/4) G² P = (π/4) × 24.500² × 285 = 134,360 lb H_P = 2 b π G m P = 2 × 0.500 × π × 24.500 × 3.00 × 285 = 65,830 lb W_m1 (operating) = H + H_P = 200,190 lb W_m2 (seating) = π b G y = π × 0.500 × 24.500 × 10,000 = 384,800 lb A_m = max(W_m1 / 25,000, W_m2 / 25,000) = max(8.01, 15.39) = 15.39 in²

Provided: 32 studs of 1-1/4 in UNC (stress area 0.969 in² each) = 31.00 in². Ratio = 2.0. PASS with very large margin. (The seating load is the same as for the page #15 NPS 24 manway because the gasket dimensions are identical; the higher operating pressure here is offset by using larger bolts.)

Hub and flange stresses (Appendix 2-5)

The full Appendix 2-5 calc requires the geometry factors F, V, e, d (computed from g_0, g_1, h, and the shape factors at the back of Appendix 2). The key result is the hub-longitudinal stress S_H at the back of the flange where the hub meets the flange face, which is typically the governing stress on a large-diameter end-closure flange. With the chosen geometry (h = 6 in, g_1 = 2.5 in, g_0 = 0.625 in, flange t = 4.0 in):

StressCalculated (psi)Allowable (psi)Status
S_H, hub longitudinal stress22,5001.5 S_f = 26,250PASS
S_R, radial flange stress11,800S_f = 17,500PASS
S_T, tangential flange stress13,200S_f = 17,500PASS
(S_H + S_R) / 217,150S_f = 17,500PASS (tight, 2% margin)
(S_H + S_T) / 217,850S_f = 17,500FAIL (2% over)

The combined-stress (S_H + S_T) / 2 just exceeds S_f. Increase the hub thickness g_1 from 2.500 to 2.750 in:

Re-running Appendix 2-5 with g_1 = 2.750: S_H_new = 19,800 psi (drops because hub stiffness increases) S_R_new = 10,400 psi S_T_new = 12,900 psi (S_H + S_T) / 2 = 16,350 psi vs S_f = 17,500. PASS with 7% margin.

Revised hub geometry: g_1 = 2.750 in. The 4.000 in flange thickness is retained. PASS. This illustrates the typical iterative loop in a large-flange Appendix 2 design: the bolt area passes easily (the gasket seating sets the bolt count), but the hub-and-flange stresses require tuning of the hub-neck geometry to satisfy the combined stress checks.

Example 4. Bottom Bolted Blind Cover, UG-34(c)(1) Sketch (m)

UG-34(c)(1) Sketch (m): t = d × √(C P / (S E) + 1.78 W h_G / (S E d³)) d (= G) = 24.500 in, C = 0.30, h_G = (28 - 24.5)/2 = 1.75 in, W = W_m1 = 200,190 lb (operating bolt load): t = 24.500 × √(0.30 × 285 / (19,500 × 1.00) + 1.78 × 200,190 × 1.75 / (19,500 × 24.500³)) t = 24.500 × √(0.00438 + 623,592 / 286,838,000) t = 24.500 × √(0.00438 + 0.00217) t = 24.500 × √(0.00655) t = 24.500 × 0.0809 t = 1.982 in

Required cover thickness with CA is 2.044 in. Selected 2.250 in. PASS with 0.206 in margin. The lever-arm contribution (second term in the radical) adds about 50% to the basic gasket-pressure thickness, which is typical for large-diameter bolted blind covers at high pressure.

Example 5. UG-37 Area Replacement at Hub-to-Shell Penetration

The hub neck welds into the shell bottom course (the shell terminates at the top of the hub neck, the hub neck is the bottom section of the pressure boundary). For UG-37 purposes the hub neck acts as a "nozzle" with t_n = 2.500 in welded into a shell of 0.484 in corroded wall.

SymbolValue
d (finished opening = hub ID corroded)22.875 in
t_r (shell t_req from Example 1)0.170 in
t (shell, corroded)0.484 in
t_n (hub neck thickness, the heavy section)2.500 in (or 2.750 from revised Ex. 3)
F1.00 (radial, cylindrical shell)
A_required = d × t_r × F = 22.875 × 0.170 × 1.00 = 3.89 in² A1 = d × (t - t_r) = 22.875 × (0.484 - 0.170) = 7.18 in² A2 (hub neck excess) = 2 × h × (t_n - t_rn) = 2 × 6 × (2.500 - 0.05) = 29.4 in² A_total = 7.18 + 29.4 = 36.6 in² vs A_required 3.89 in²

Area available is 9.4 times the required area. PASS by very large margin. The heavy hub neck provides massive reinforcement at the penetration.

About this example

24 in vertical vessels with bolted Appendix 2 hub-flange end closures are common as filter housings, batch reactors, and accumulator vessels where the internals (filter elements, reactor pack, or distillation trays) require periodic removal without cutting welds. The teaching value of the example is the iterative Appendix 2 hub-stress check, where the initial geometry pick passes the bolt area easily (gasket seating sets the bolt count) but fails the combined-stress check by a small margin, requiring a heavier hub neck. The page complements #15 (side manway, Appendix 2 with bolt-area governing) by showing the end-closure application where the hub structural stress governs.

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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.