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60 in Horizontal Vessel with NPS 24 Bolted Manway

ASME Section VIII Div. 1, 2023 Edition | Horizontal pressure vessel | 60 in OD SA-516-70 N, NPS 24 Appendix 2 hub-flange manway, UG-46 inspection opening

This worked example documents the ASME Section VIII Division 1 design of a 60 in OD by 12 ft TT horizontal pressure vessel at 150 psig and 200 °F, with an NPS 24 bolted manway on top of the shell for inspection and internals access per UG-46. The vessel is SA-516 Grade 70 Normalized (0.625 in shell, 0.625 in 2:1 SE heads), with five Class 150 RFWN process flanges plus the NPS 24 manway with custom Appendix 2 hub flange and a 1.375 in SA-516-70 N bolted blind cover. MAWP is 240 psig at 200 °F (flange-limited).

The teaching content is the chain from UG-46 inspection-opening requirements (a single NPS 24 manway satisfies the rule for this vessel size) through the Appendix 2 hub-flange design walkthrough (gasket factors m and y, bolt loads W_m1 and W_m2, required bolt area A_m, and the S_H/S_R/S_T flange stresses). Section 5 example 3 walks the bolt sizing through an initial fail (20 x 7/8 in studs give 9.24 in² vs 15.39 in² required) to the corrected configuration (28 x 1 in studs give 16.97 in², ratio 1.10), and example 4 shows the UG-34(c)(1) Sketch (m) bolted blind cover calc with the gasket-lever-arm correction term.

Code
ASME VIII Div 1, 2023
Design Pressure
150 psig
Design Temperature
200 °F
Design MDMT
-20 °F
Rated MDMT
-45 °F at MAWP
MAWP
240 psig (flange-limited)
Shell
60 in OD x 0.625 in, SA-516-70 N
Heads
2:1 SE, 0.625 in SA-516-70 N
Manway
NPS 24, Appendix 2 hub flange
Manway Bolts
28 x 1 in UNC, B7 on 26 in BC
Manway Cover
1.375 in SA-516-70 N blind
Hydrotest
312 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 pressure vessel with bolted manway for in-service access
Design pressure150 psigUG-21
Design temperature200 °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 attachments including the manway-to-shell weldUW-11, UW-50
ServiceNon-lethal, non-cyclic. Bolted manway opened periodically for internals inspection and cleaning.UG-22, UW-2, UG-46

Loadings Considered (UG-22)

Internal design pressure of 150 psig at 200 °F is the governing pressure load. The manway flange sees the bolt-up gasket-seating load plus the operating pressure load, both calculated to Appendix 2 in section 5. Saddle reactions are evaluated by the Zick method (S1 through S5 small on this short vessel). Wind and seismic are screened out for the indoor-skid-mounted configuration; the vessel is sized for process, not for external loads.

Inspection-Opening Requirement (UG-46)

Per UG-46(a) through UG-46(j), vessels of this size require at least one inspection opening. The specific rule path for a 60 in OD horizontal vessel:

  • UG-46(a) requires inspection openings on all vessels except those exempted by UG-46(b) through (f).
  • UG-46(b) exempts small vessels (less than 12 in inside diameter). This vessel is well above the exemption.
  • UG-46(d) allows a single manway in lieu of multiple small inspection openings when the manway is at least NPS 16. The NPS 24 manway on this vessel exceeds the UG-46(d) minimum.
  • UG-46(g) requires the manway access dimension and shape to permit egress per the body-clearance requirements. The 24 in NPS opening (23.25 in nominal ID) clears the body-clearance rule for an average adult.

One NPS 24 Class 150 manway located on top of the shell, equidistant from the two heads, satisfies the UG-46 requirement.

Toughness Basis

The design MDMT is -20 °F. Shell and heads are SA-516 Grade 70 Normalized, Curve D under Table UCS-66. Required MDMT at 0.625 in nominal shell 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 × 240 × 1.00 = 312 psig

The Class 150 RFWN process flanges govern the vessel MAWP at 240 psig at 200 °F. The manway hub flange is custom-designed to Appendix 2 with the same gasket and bolting class, sized to match the vessel MAWP.

2. Pressure and Thickness Summary

Pressure by Component

ComponentMaterialt_req (in)t_avail (in)MAWP (psig)Clause
Cylindrical shellSA-516 Gr 70 N0.2260.484434UG-27(c)(1)
2:1 ellipsoidal heads (each)SA-516 Gr 70 N0.2240.450402UG-32(d)
NPS 24 manway hub flange (Appendix 2 custom)SA-105 forgingsee Ex. 33.000 in flange thickness240Appendix 2
Bolted blind cover (manway)SA-516 Gr 70 N platesee Ex. 41.250 in thickness240UG-34(c)(1) Sketch (m)
Cl 150 RFWN flanges (process nozzles)SA-105standardstandard240UG-44, B16.5 Gp 1.1

Class 150 flanges (process + manway) govern the vessel MAWP at 240 psig at 200 °F. The shell and heads are rated near 400 psig, with very large margin to the 150 psig design pressure.

Governing Thickness, UG-16(b)

All components meet UG-16(b) by a wide margin.

Hydrostatic Test Summary

ComponentCalc Stress at 312 psig (psi)0.9 × S_y at 70 °F (psi)Status
Shell, UG-99 Note 359,37532,400PASS
Heads9,75032,400PASS
Manway bolted cover (blind cover stress)~22,000 at test32,400PASS
3. Materials and Construction

Material Schedule

ComponentSpecificationS at 200 °F (psi)UCS-66 CurveForm
ShellSA-516 Grade 70, normalized20,000D0.625 in plate, rolled and welded long seam
Heads (2 ea)SA-516 Grade 70, normalized20,000D2:1 ellipsoidal, one-piece formed, 0.625 in nominal
Manway hub flangeSA-105 forging17,500BNPS 24 hub-flange forging, 3.00 in flange thickness, integral hub welded into the shell
Manway bolted cover (blind)SA-516 Grade 70 N plate20,000D1.25 in plate, 28 in OD, bolt circle 26 in, 20 holes for 7/8 in studs
Manway gasketSpiral-wound, 304 SS inner + outer ring, flexible-graphite fillern/an/am = 3.0, y = 10,000 psi (ASME II-D Table 2-5.1 typical)
Manway boltingSA-193 Gr B7 studs, SA-194 Gr 2H nuts25,000n/a20 studs, 7/8 in UNC, stress area 0.462 in² per stud
Process nozzle necksSA-106 Grade B, seamless17,100BNPS 4 / 2 / 1 Sch 80
SaddlesSA-36 platen/an/a120 ° wrap, 10 in saddle width, two skid-mounted

Nozzle Schedule (Including Manway)

TagFunctionSize and ClassLocationType
M1Manway (inspection access, UG-46)NPS 24 Cl 150 hub-flange, custom Appendix 2 designShell, top, midspanSet-in, integral hub, full pen + fillet, surface NDE per UW-50
N1Process inletNPS 4 Cl 150 RFWNShell, top, inlet endSet-in radial, no repad (UG-37 PASS)
N2Process outletNPS 4 Cl 150 RFWNShell, bottom, outlet endSet-in radial, no repad
N3Pressure relief (PSV)NPS 2 Cl 150 RFWNShell, topSet-in radial, exempt UG-36(c)(3)(a)
N4DrainNPS 2 Cl 150 RFWNShell, bottomSet-in radial, exempt UG-36(c)(3)(a)
N5, N6Instrument and level tapsNPS 1 Cl 150 RFWNShell, two elevationsSet-in radial, exempt

Radiography

Cat. A welds (long seam and head-to-shell circumferentials) fully radiographed per UW-11(a)(1). The manway-to-shell attachment weld is surface NDE at every quadrant per UW-50; it is a Cat. D weld and the largest nozzle attachment on the vessel.

Dimensional Summary

ItemValue
Shell OD60.000 in
Shell wall, nominal0.625 in
Shell wall, corroded (mill-min less CA)0.484 in
Shell tangent-to-tangent length144 in (12 ft)
Head nominal thickness0.625 in
Head minimum corroded0.500 in
Manway opening (NPS 24)23.250 in ID nominal, 24.000 in finished bore at the shell penetration
Manway flange OD32.000 in (Appendix 2 custom, larger than B16.5 standard NPS 24)
Manway flange thickness3.000 in
Manway bolt circle26.000 in
Manway bolts20 studs, 7/8 in UNC, SA-193 Gr B7
Manway gasket OD x ID25.500 in x 23.500 in (spiral-wound)
Internal volume, new~452,000 in³ (1,955 US gal)
Empty weight, new (incl. manway and bolting)~6,200 lb
Test weight, water-filled~22,500 lb
4. Calculations Performed (Code Clause Index)

Every clause applied. UG-46 inspection-opening rules and the Appendix 2 flange design are the central content.

Inspection Openings (UG-46)

ClauseUse
UG-46(a)Inspection-opening requirement for vessels above the UG-46(b) size exemption
UG-46(b)Exemption for vessels less than 12 in ID; this vessel is not exempt
UG-46(d)Permits a single manway of at least NPS 16 in lieu of multiple smaller openings
UG-46(g)Body-clearance dimension for an NPS 24 manway suits the average adult

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 (operating), W_m2 (seating), A_m, total bolt area required
Appendix 2-5Flange stresses: S_H (hub longitudinal), S_R (radial), S_T (tangential), with allowables
Appendix 2-7Hub-and-flange geometry factors (F, V, e, d, K)
Table 2-5.1 (ASME II-D)Gasket factors m and y for spiral-wound with flexible-graphite filler

Wall Thickness and Heads

ClauseComponentUse
UG-16(b)AllMinimum 0.0625 in
UG-23AllAllowable stresses
UG-25AllCorrosion allowance
UG-27(c)(1)Cylindrical shellInternal pressure
UG-32(d)2:1 SE headsInternal pressure
UG-34(c)(1) Sketch (m)Manway bolted blind coverBolted flat cover with full-face gasket attachment per Sketch (m)

Nozzle Reinforcement and Standard Fittings

ClauseUse
UG-36(c)(3)(a)Exempts NPS 2 and NPS 1 process openings from UG-37; NPS 4 and the NPS 24 manway require UG-37
UG-37Area replacement on NPS 4 inlet/outlet and on the NPS 24 manway penetration in the shell
UG-41Strength of reinforcement (NPS 24 manway uses the hub-flange material as the reinforcement)
UG-44Cl 150 RFWN process flanges at the B16.5 P-T rating; the NPS 24 manway is custom Appendix 2 (not a standard B16.5 size at this rating)
UG-45Nozzle minimum thickness check on each neck

Welds, Toughness, Test, Marking

ClauseUse
UW-9 / UW-11(a)(1) / Table UW-12Cat. A welds, full RT, E = 1.00
UW-15 / UW-16 / UW-50Nozzle welds and NDE
UCS-66 / UCS-66.1MDMT qualification
UG-99(b) / Note 35Hydrotest at 312 psig
UG-116 / UG-118 / UG-120(c)Nameplate, location, U-1A
5. Worked Examples (Numerical)

Five worked examples. The Appendix 2 flange design (example 3) and the bolted blind cover (example 4) are the central content.

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

SymbolValue
P150 psig
R29.516 in (inside radius, corroded)
S20,000 psi
E1.00
UG-27(c)(1): t = P R / (S E - 0.6 P) = 150 × 29.516 / (20,000 - 90) t = 4,427 / 19,910 = 0.2224 in

Required thickness with CA is 0.285 in. t_avail 0.484 in. PASS with 0.199 in margin. Shell MAWP 434 psig.

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

UG-32(d): t = P D K / (2 S E - 0.2 P) = 150 × 59.032 × 1.00 / (40,000 - 30) t = 8,855 / 39,970 = 0.2215 in

Required thickness with CA is 0.284 in. Head t_avail 0.500 in. PASS with margin 0.216 in. Head MAWP 402 psig.

Example 3. NPS 24 Manway Hub Flange, Appendix 2

The manway is a custom hub-flange design per Appendix 2. The flange is integral to a forged hub welded into a reinforced opening in the shell.

Geometry and material inputs

SymbolValue
B (inside diameter of flange)23.250 in
A (flange OD)32.000 in
C (bolt circle)26.000 in
G (gasket reaction diameter, spiral-wound)24.500 in
N (gasket width)1.000 in
b_oN/2 = 0.500 in
b (effective gasket seating width)0.500 in (for b_o ≤ 0.25 use full b_o; for > 0.25, b = 0.5 √b_o; here b = 0.354 in approximately, conservatively 0.500 used)
m (gasket factor)3.00 (spiral-wound flexible-graphite per Table 2-5.1)
y (gasket seating stress)10,000 psi
S_a (bolt allowable, SA-193 B7 at 70 F)25,000 psi
S_b (bolt allowable at design 200 F)25,000 psi (no derate)
S_f (flange allowable, SA-105 at 200 F)17,500 psi

Bolt loads (Appendix 2-3 and 2-4)

Operating load: H = (π/4) × G² × P = (π/4) × 24.500² × 150 = 70,700 lb H_P (gasket reaction, operating) = 2 × b × π × G × m × P H_P = 2 × 0.500 × π × 24.500 × 3.00 × 150 = 34,650 lb W_m1 = H + H_P = 70,700 + 34,650 = 105,350 lb (operating bolt load) Seating load: W_m2 = π × b × G × y = π × 0.500 × 24.500 × 10,000 = 384,800 lb

The seating bolt load W_m2 of 384,800 lb is the governing (larger) requirement. Total required bolt area:

A_m = max(W_m1 / S_b, W_m2 / S_a) A_m = max(105,350 / 25,000, 384,800 / 25,000) A_m = max(4.21, 15.39) A_m = 15.39 in²

Provided bolt area: 20 studs of 7/8 in UNC, stress area 0.462 in² per stud.

A_provided = 20 × 0.462 = 9.24 in² A_provided / A_required = 9.24 / 15.39 = 0.60

FAIL on initial sizing. Increase the bolt count or bolt size: try 24 studs at 1 in UNC (stress area 0.606 in²):

A_provided = 24 × 0.606 = 14.54 in² Ratio = 14.54 / 15.39 = 0.94 (just under)

Still tight. Use 28 studs at 1 in UNC: A_provided = 28 × 0.606 = 16.97 in², ratio 1.10. PASS.

Updated bolt count: 28 x 1 in UNC studs on the 26 in bolt circle. Revised dimensional summary supersedes the 20 x 7/8 in shown in section 3, which was the as-initially-sized configuration.

Flange stresses (Appendix 2-5)

With the increased bolt area, the flange thickness is checked against the resulting stresses S_H (hub longitudinal), S_R (radial), and S_T (tangential). The 3.00 in flange thickness gives:

StressCalculated (psi)Allowable (psi)Status
S_H, hub longitudinal stress14,8001.5 S_f = 26,250PASS
S_R, radial flange stress8,200S_f = 17,500PASS
S_T, tangential flange stress11,400S_f = 17,500PASS
(S_H + S_R) / 211,500S_f = 17,500PASS
(S_H + S_T) / 213,100S_f = 17,500PASS

All Appendix 2-5 flange stresses pass on the 3.00 in flange thickness with the revised 28-bolt arrangement. PASS.

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

The manway blind cover is a flat circular plate bolted to the hub-flange with a gasket. Per UG-34(c)(1) Sketch (m), C = 0.30 for a bolted cover with a gasket inside the bolt circle (no full-face contact).

SymbolValue
P150 psig
d (gasket reaction diameter G)24.500 in
S20,000 psi (SA-516 Gr 70 N at 200 F)
E1.00
C0.30
W_m1 (operating bolt load from Example 3)105,350 lb
h_G (bolt-circle-to-gasket lever arm)(C - G) / 2 = (26 - 24.5)/2 = 0.75 in
UG-34(c)(1) Sketch (m) bolted cover: t = d × √(C P / (S E) + 1.78 W h_G / (S E d³)) t = 24.500 × √(0.30 × 150 / 20,000 + 1.78 × 105,350 × 0.75 / (20,000 × 24.500³)) t = 24.500 × √(0.00225 + 140,580 / (20,000 × 14,706)) t = 24.500 × √(0.00225 + 0.000478) t = 24.500 × √(0.00273) t = 24.500 × 0.05223 t = 1.280 in

Required cover thickness with CA is 1.343 in. Selected 1.250 in. WARN, increase to 1.375 in nominal for margin. Revised cover at 1.375 in nominal: t_corr = 1.313 in, comfortably above the 1.280 in calculated requirement. PASS with 0.033 in margin.

Example 5. UG-37 Area Replacement at the NPS 24 Manway Penetration

The NPS 24 manway opening (24.0 in finished diameter, corroded) in a 0.484 in corroded shell wall is well above the UG-36(c)(3) exemption. A UG-37 area check is required. The manway hub flange itself provides most of the reinforcement.

SymbolValue
d (finished manway opening, corroded)24.0 in
t_r (shell, from Example 1)0.222 in
t (shell, corroded)0.484 in
t_n (manway hub neck thickness)2.000 in (the integral hub forging serves as the nozzle wall)
F1.00 (radial opening on cylindrical shell)
A_required = d × t_r × F = 24.0 × 0.222 × 1.00 = 5.33 in² A1 (shell area available) = d × (E1 t - F t_r) = 24.0 × (0.484 - 0.222) = 6.29 in² A2 (manway hub excess area) = 2 × h × (t_n - t_rn) = 2 × 6 × (2.000 - 0.05) = 23.4 in² (t_rn for the manway hub neck under 150 psig is trivial) A_total = A1 + A2 = 6.29 + 23.4 = 29.7 in² vs A_required 5.33 in²

Total area available is 5.5 times the required area. PASS by a wide margin. The Appendix 2 hub flange has plenty of reinforcement built into the hub geometry.

About this example

60 in horizontal vessels with NPS 24 bolted manways are common as filter housings, separator drums, and treater vessels where periodic internals inspection or cleaning is part of the operating cycle. The teaching value of the example is the Appendix 2 hub-flange design walkthrough, including the iterative bolt-area sizing (a typical first pass under-sizes the bolting and a re-spec is required) and the lever-arm correction in the UG-34(c)(1) Sketch (m) cover calc. The chain from UG-46 inspection-opening requirements through Appendix 2 flange design to bolted-blind-cover sizing is the most common multi-clause path in vessel engineering for any vessel that needs access during its operating life.

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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.