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24 in Hemispherical-Head Reactor at 1,000 psig

ASME Section VIII Div. 1, 2023 Edition | Vertical reactor | 24 in OD SA-516-70 N shell, hemispherical heads both ends, 1,000 psig at 200 F

This worked example documents the ASME Section VIII Division 1 design of a 24 in OD vertical reactor at 1,000 psig and 200 °F, with hemispherical heads at both ends. The vessel is SA-516 Grade 70 Normalized: a 0.875 in nominal shell and 0.500 in nominal hemispherical heads, with Class 600 RFWN flanges on the four process nozzles. Vessel MAWP is 1,200 psig (shell-governed); the hemispherical heads are rated 1,360 psig at the in-service thickness.

The teaching content is the dramatic thickness contrast among the curved head types at high pressure. Section 5 example 3 compares hemispherical (0.500 in nominal, UG-32(f)), 2:1 SE (0.750 in nominal, UG-32(d)), and F&D torispherical (1.250 in nominal, UG-32(c)) on the same 24 in shell at the same 1,000 psig design point. The hemi head requires half the thickness of the SE and a quarter of the F&D, but adds 14 in of overall vessel height (D/2 per end). At this pressure the hemi is the natural choice when overall height is not a hard constraint. Pairs with the moderate-pressure head comparison on the 48 in OD vessel page.

Code
ASME VIII Div 1, 2023
Design Pressure
1,000 psig
Design Temperature
200 °F
Design MDMT
-20 °F
Rated MDMT
-35 °F at MAWP
MAWP
1,200 psig (shell)
Shell
24 in OD x 0.875 in, SA-516-70 N
Heads
Hemispherical, 0.500 in SA-516-70 N
Corrosion Allowance
0.0625 in
Flanges
B16.5 Cl 600 RFWN
Empty Weight, New
1,180 lb
Hydrotest
1,560 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 reactor, hemispherical heads both ends
Design pressure1,000 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 hemi)UW-12
RadiographyFull RT on Cat. A welds, surface NDE on nozzle weldsUW-11, UW-50
ServiceNon-lethal, non-cyclic, gas-phase or supercritical reaction serviceUG-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 1,000 psig at 200 °F.
  • Weight of the vessel and its contents (small, dense reactor pack or catalyst bed).
  • Two welded support lugs at the lower head-to-shell weld; the vessel is small and skid-mounted, so wind and seismic are screened out for this configuration.

Non-cyclic per UG-22(e).

Toughness Basis

The design MDMT is -20 °F at full pressure. The shell and heads are SA-516 Grade 70 Normalized, Curve D under Table UCS-66. Required MDMT at the shell thickness (0.875 in nominal) is approximately -35 °F at no impact testing, which is colder than the design MDMT requirement.

Hydrostatic Test Basis

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

P_test = 1.3 × MAWP × LSR = 1.3 × 1,200 × 1.00 = 1,560 psig

SA-516 Grade 70 does not derate below 300 °F so the material LSR is 1.00. The Class 600 RFWN flanges have a 70 °F rating of 1,500 psig, so the test pressure is just over the cold flange rating; the flange stud loading is checked in the hydrotest summary against the 0.9 S_y limit and passes by inspection.

2. Pressure and Thickness Summary

Pressure by Component

ComponentMaterialt_req (in)t_avail (in)MAWP (psig)Clause
Cylindrical shellSA-516 Gr 70 N0.5820.7031,200UG-27(c)(1)
Hemispherical heads (top and bottom)SA-516 Gr 70 N0.2840.3881,360UG-32(f)
Cl 600 RFWN flanges (process)SA-105standardstandard1,440UG-44, B16.5 Gp 1.1 at 200 F
NPS 2 inlet/outlet, NPS 1 instrumentSA-106 Gr B< 0.10> 0.30matches shellUG-27(c)(1)

The cylindrical shell governs the vessel MAWP at 1,200 psig. The hemispherical heads are rated 1,360 psig at the same in-service thickness (0.388 in formed-corroded), 160 psig above the shell. The high-pressure design point is what makes the hemispherical head the natural choice on this vessel; an F&D head at 1,000 psig would require about 2.5 in of plate and a 2:1 SE head about 1.0 in. See worked example 3 for the comparison.

Governing Thickness, UG-16(b)

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

Hydrostatic Test Summary

ComponentCalc Stress at 1,560 psig (psi)0.9 × S_y at 70 °F (psi)Status
Shell, UG-99 Note 3525,33032,400 (SA-516-70 N)PASS
Hemispherical heads22,75032,400PASS
Cl 600 flange (B16.5 rating)1,560 psig (above 1,500 cold rating)standard productPASS (stud check)
3. Materials and Construction

Material Schedule

ComponentSpecificationS at 200 °F (psi)UCS-66 CurveForm
ShellSA-516 Grade 70, normalized20,000D0.875 in plate, rolled and welded long seam
Top and bottom hemispherical headsSA-516 Grade 70, normalized20,000D0.500 in plate, one-piece formed, hemispherical to a 24 in OD skirt
Nozzle necksSA-106 Grade B, seamless17,100BNPS 2 / 1 Schedule 80 or thicker
FlangesSA-10517,500BASME B16.5 RFWN Class 600, all process nozzles
BoltingSA-193 Gr B7 studs, SA-194 Gr 2H nuts25,000n/astandard B16.5 stud-and-nut sets
Support lugsSA-516 Grade 70 platen/an/aTwo welded lugs at the lower head-to-shell circumferential weld

Nozzle Schedule

TagFunctionSize and ClassLocationTypeWeld
N1Process inletNPS 2 Cl 600 RFWN, Sch 160 neckTop hemi headSet-in radial, no repad (UG-37 PASS)Full pen + fillet per UW-16(f)
N2Process outletNPS 2 Cl 600 RFWN, Sch 160 neckBottom hemi headSet-in radial, no repadFull pen + fillet per UW-16(f)
N3Pressure relief (PSV)NPS 1 Cl 600 RFWN, Sch 160 neckShell, topSet-in radial, exempt UG-36(c)(3)(a)Full pen + fillet per UW-16(f)
N4Instrument tapNPS 1 Class 6000 threaded couplingShellSet-on, exempt UG-36(c)(3)(a)Full pen + fillet per UW-16(f)

All openings are below the UG-36(c)(3)(a) 3.5 in finished-diameter exemption limit on a 0.703 in corroded shell. The NPS 2 inlet and outlet (2.067 in finished bore) are well within the exemption.

Radiography

Category A welds (long seam and head-to-shell circumferentials) are fully radiographed per UW-11(a)(1). The hemispherical-to-shell joint is a Category A circumferential and receives 100% RT plus surface NDE on the OD per UW-50 to confirm full penetration. Nozzle attachment welds are MT or PT per UW-50.

Dimensional Summary

ItemValue
Shell OD24.000 in
Shell wall, nominal0.875 in
Shell wall, mill-min (-12.5%)0.766 in
Shell wall, corroded (mill-min less CA)0.703 in
Shell tangent-to-tangent length60 in (5 ft)
Head nominal thickness, hemispherical0.500 in
Head minimum corroded (after 10% forming thinning + CA)0.388 in
Head inside depth, D/2 hemispherical11.30 in
Overall tangent-to-crown height (shell + 2 hemi heads)60 + 2 × 11.30 = 82.6 in
Internal volume, new (shell + 2 hemi heads)30,000 in³ (130 US gal)
Empty weight, new1,180 lb
Empty weight, corroded1,090 lb
Test weight, water-filled2,265 lb
4. Calculations Performed (Code Clause Index)

Every clause applied. The hemispherical-head walkthrough (UG-32(f)) is the central content.

Wall Thickness

ClauseComponentUse
UG-16(b)AllMinimum 0.0625 in
UG-23AllAllowable stresses at design temperature
UG-25AllCorrosion allowance 0.0625 in
UG-27(c)(1)Cylindrical shellInternal pressure, circumferential stress
UG-32(c)Comparison only (F&D option)Reference in head-comparison summary
UG-32(d)Comparison only (2:1 SE option)Reference in head-comparison summary
UG-32(f)Hemispherical heads (as-built)Required thickness, L = inside crown radius

Nozzle Reinforcement

ClauseUse
UG-36(c)(3)(a)Exempts all NPS 2 and NPS 1 openings from detailed UG-37
UG-37Area replacement, run as verification on the NPS 2 inlet (PASS by large margin)
UG-43(a)Threaded openings on the instrument tap
UG-44Cl 600 RFWN flanges accepted at 1,440 psig at 200 F
UG-45Nozzle min thickness check

Welds, Toughness, Test, Marking

ClauseUse
UW-9 / UW-11(a)(1) / Table UW-12Cat. A weld design, full RT, E = 1.00
UW-15 / UW-16 / UW-50Nozzle attachment welds and NDE
UCS-66 / UCS-66.1MDMT qualification
UG-99(b) / Note 35Hydrotest at 1,560 psig, stress under 0.9 S_y
UG-116 / UG-118 / UG-120(c)Nameplate, location, U-1A
5. Worked Examples (Numerical)

Five worked examples. The hemispherical-head calc (example 2) and the head-type comparison at 1,000 psig (example 3) are the central teaching content.

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

SymbolValueSource
P1,000 psigDesign pressure
R11.297 inInside radius, corroded: (24 - 2 × 0.703) / 2
S20,000 psiSA-516 Gr 70 at 200 °F
E1.00Full RT long seam
UG-27(c)(1): t = P R / (S E - 0.6 P) t = 1,000 × 11.297 / (20,000 - 600) t = 11,297 / 19,400 t = 0.5823 in

Required thickness with CA is 0.645 in. Mill-min supplied is 0.766 in (0.875 nom less 12.5%), corroded to 0.703 in. PASS with 0.058 in margin. Shell MAWP at corroded thickness is 1,200 psig.

Example 2. Hemispherical Head Thickness, UG-32(f)

SymbolValueSource
P1,000 psigDesign pressure
L11.297 inInside crown radius (equals shell R_corr for a hemi head)
S20,000 psiSA-516 Gr 70 at 200 °F
E1.00One-piece formed head
UG-32(f): t = P L / (2 S E - 0.2 P) t = 1,000 × 11.297 / (40,000 - 200) t = 11,297 / 39,800 t = 0.2839 in

Required thickness with CA is 0.346 in. Nominal head ordered at 0.500 in; after 10% forming thinning and CA, the in-service minimum is 0.388 in. PASS with 0.042 in margin.

Hemi head MAWP at 0.388 in formed-corroded thickness: P_max = 2 S E t / (L + 0.2 t) P_max = 2 × 20,000 × 1.00 × 0.388 / (11.297 + 0.078) P_max = 15,520 / 11.375 P_max = 1,364 psig

Example 3. Head Type Comparison at 1,000 psig (Hemi vs 2:1 SE vs F&D)

The same shell could be closed by any of three curved heads. At the 1,000 psig design pressure of this vessel, the contrast is dramatic:

Head typeClauset_req (in)t_nom selected (in)Head depth (in)Single-head weight (lb)
Hemispherical (as-built)UG-32(f), t = PL/(2SE - 0.2P)0.2840.50011.3~120
2:1 SEUG-32(d), t = PDK/(2SE - 0.2P)0.5680.7505.6~160
F&D (L = OD, r = 6% OD)UG-32(c), t = MPL/(2SE - 0.2P), M = 1.751.0551.2504.2~280

The hemispherical head is half the required thickness of the 2:1 SE and a quarter of the F&D. Adding the corrosion allowance and the formed-min discount makes the practical selected nominal thickness 0.500 in for hemi, 0.750 in for SE, and 1.250 in for F&D. The hemi head is also 25 to 60 percent lighter despite being deeper. The trade-off is the overall vessel height: 11.3 in of extra height per end for hemi vs 5.6 in for SE vs 4.2 in for F&D, so the hemi adds about 14 in of overall stack height on this 5 ft tan-to-tan vessel. For a process where height is unconstrained (open-air skid mounting, reactor in a structural frame), the hemi is the natural choice at this pressure. For a process where overall height is a hard constraint (transport-by-truck, indoor mezzanine clearance), the SE or F&D is selected and the thickness penalty is accepted.

Example 4. NPS 2 Inlet Nozzle, UG-37 Area Verification

The NPS 2 inlet on the top hemispherical head is well below the UG-36(c)(3)(a) exemption limit. A UG-37 area calc is shown as verification only.

SymbolValue
d (NPS 2 ID corroded)2.192 in
t_r (head, from example 2)0.284 in
t (head, corroded formed)0.388 in
F (radial in hemispherical head)1.00
A_required = d × t_r × F = 2.192 × 0.284 × 1.00 = 0.623 in² A1 = d × (E1 t - F t_r) = 2.192 × (0.388 - 0.284) = 0.228 in² A2 (nozzle wall excess) = 2 × h × (t_n - t_rn) for Sch 160 NPS 2 (t_n ~ 0.34 in) ≈ 0.85 in² A_total ≈ 1.08 in² vs A_required 0.623 in²

PASS by 70% margin even with conservative A2 estimation. The exemption under UG-36(c)(3)(a) is the code basis; the UG-37 calc above confirms the exemption is non-binding.

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

P_test = 1.3 × MAWP × LSR P_test = 1.3 × 1,200 × 1.00 = 1,560 psig
ComponentStress at test (psi)0.9 × S_y at 70 °F (psi)Status
Shell (hoop)1,560 × 11.297 / 0.703 = 25,07032,400 (SA-516-70 N)PASS
Hemi head (membrane)1,560 × 11.297 / (2 × 0.388) = 22,71032,400PASS
Cl 600 flange stud loading at 1,560 psig (above 1,500 cold rating)20,800 (stud root area)32,400PASS

Test pressure stresses are below the 0.9 S_y limit for all pressure-boundary components. The Class 600 flange stud loading at the 1,560 psig test pressure (slightly above the 1,500 psig cold rating of the flange) is checked against the SA-193 B7 stud allowable, with the standard B16.5 stud arrangement passing by 35%.

About this example

24 in OD vertical reactors at 1,000 psig are common as small batch reactors, supercritical-fluid contactors, and high-pressure separator vessels in research and pilot-scale skids. The configuration uses hemispherical heads because the high design pressure makes the thickness savings of the hemi shape (about 50% lighter than 2:1 SE and 75% lighter than F&D at this pressure) outweigh the added height. The teaching value of the example is the side-by-side thickness comparison among the three curved head types at high pressure, which makes the case for hemi heads above approximately 600 psig on vessels in this size range.

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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.