SAMPLE
Piping Toolset — Calculation Report
generated by calc-core · 2026-11-12

ASME B31.1 Safety Valve Reaction Force Calculator (Appendix II, Open Discharge) — Sample Report

ProjectSample Project — Demonstration Only Job No.SAMPLE-001 Client—
CalculationASME B31.1 Safety Valve Reaction Force Calculator (Appendix II, Open Discharge) Calc byPiping Toolset (calc-core) Checked byUNCHECKED — sample
Date2026-11-12 Rev0 BasisASME B31.1-2026 (unchanged from 2024) Nonmandatory Appendix II — ¶II-2.2.1 exit state, ¶II-2.3.1.1 open-discharge reaction F1 = ṁV1/gc + (P1 − Pa)A1 with ṁ = 1.11 × stamped capacity; DLF applied per ¶II-3.5.1.3 (Table II-2.2.1-1 steam constants embedded)

1 · Design inputs

Hot reheat safety valve on the reheater outlet lead, set at 750 psig with steam at 1,000°F, stamped 400,000 lb/hr, discharging through an NPS 10 Sch 40 elbow (10.02 in ID, 78.85 in² flow area) into a separate vent pipe. ASSUMED inputs for this example: ho = 1,512 Btu/lbm, DLF = 2.0, and round stand-in steam constants a = 820 Btu/lbm and b = 4.3. The stand-ins are not the Table II-2.2.1-1 values: read a and b from your own copy for the steam condition and exit-pressure range, or use the picker on the card.

Stamped relieving capacity400,000lb/hr
Stagnation enthalpy ho (ASSUMED)1,512Btu/lbm
Steam constant a (ASSUMED stand-in)820Btu/lbm
Steam constant b (ASSUMED stand-in)4.3—
Elbow exit area A178.85in²
Atmospheric pressure Pa14.7psia
Dynamic load factor DLF (ASSUMED)2.0—

2 · Method

Conditions at the discharge elbow exit, Point 1, B31.1 Nonmandatory Appendix II ¶II-2.2.1(a):

V1 = √( 2·gc·J·(ho − a) / (2b − 1) )

P1 = (ṁ / A1)·((b − 1) / b)·√( 2·(ho − a)·J / (gc·(2b − 1)) )

Reaction force at Point 1, ¶II-2.3.1.1, and the design load:

F1 = ṁ·V1 / gc + (P1 − Pa)·A1

ṁ = 1.11 × stamped relieving capacity

Fdesign = F1 × DLF

The force has two parts. The first is momentum: mass flow times exit velocity. The second is pressure: the flow leaves the elbow choked, so the static pressure at the exit plane is above atmospheric and acts over the exit area. The Appendix writes the mass flow as the capacity stamped on the valve times 1.11, with ṁ in lbm/sec, and the calculator does that conversion from lb/hr. ho is the stagnation enthalpy at the valve inlet, from steam tables at the relieving condition. a and b are the two constants of Table II-2.2.1-1, selected by steam condition and by the range the exit pressure falls in, so check the computed P1 against the range of the row you used. The constants gc = 32.2 lbm-ft/lbf-sec² and J = 778.16 ft-lbf/Btu are as printed in the Appendix. US customary units throughout: Btu/lbm, in², psia, lbf. The dynamic load factor covers the suddenness of the load and is your input.

3 · Calculation

  1. Mass flow, ¶II-2.3.1.1: ṁ = 1.11 × 400,000 / 3,600 = 123.33 lbm/s.
  2. Enthalpy term: ho − a = 1,512 − 820 = 692 Btu/lbm; 2b − 1 = 7.6.
  3. Exit velocity: V1 = √(2 × 32.2 × 778.16 × 692 / 7.6) = √4,562,966 = 2,136.1 ft/s.
  4. Exit pressure: P1 = (123.33 / 78.85) × (3.3 / 4.3) × √(2 × 692 × 778.16 / (32.2 × 7.6)) = 1.5642 × 0.7674 × 66.339 = 79.63 psia. That sits inside the pressure range of the table row the stand-ins represent.
  5. Momentum term: ṁ·V1 / gc = 123.33 × 2,136.1 / 32.2 = 8,181.8 lbf.
  6. Pressure term: (P1 − Pa)·A1 = (79.63 − 14.7) × 78.85 = 5,120.0 lbf.
  7. Steady reaction: F1 = 8,181.8 + 5,120.0 = 13,302 lbf.
  8. Design load: F1 × DLF = 13,302 × 2.0 = 26,603 lbf, acting on the elbow opposite the jet.

4 · Results COMPUTED

F1 × DLF — design reaction force26,603lbf
F1 — steady-state reaction force13,302lbf
V1 — exit velocity2,136.1ft/s
P1 — exit static pressure79.63psia
ṁ — mass flow123.33lbm/s

5 · Verification statement

The result values above are locked as fixture b311-reaction.json, case “hot reheat safety valve, 400,000 lb/hr stamped, h0=1512 Btu/lbm, NPS 10 Sch 40 elbow A1=78.85 in², illustrative a=820 b=4.3, DLF 2.0”, tolerance 0.001, in the calc-core continuous verification gate (see https://pipingtoolset.com/trust/validation.html). Allowable-stress and factor data are user-supplied inputs; citations: ASME B31.1-2026, Power Piping, Nonmandatory Appendix II — ¶II-2.2.1(a), pressure P1 and velocity V1 at the discharge elbow outlet; Figure II-2.2.1-1; Table II-2.2.1-1, values of a and b by steam condition (typed from your copy, or autofilled by the picker on the card and cited there). These paragraphs and the table read the same in B31.1-2024. · ASME B31.1-2026 Appendix II ¶II-2.3.1.1 — reaction force F1 at the discharge elbow, with mass flow taken as the relieving capacity stamped on the valve × 1.11, and a dynamic load factor to be applied. · ASME B31.1-2026 Appendix II ¶II-3.5.1.1 and ¶II-3.5.1.3 — reaction moments and the branch-connection floor DLF × F1 × Lo; dynamic load factor from the installation period and Figure II-3.5.1.3-2, never taken less than 1.1. · ASME B31.1-2026 Appendix II ¶II-1.2 (open and closed discharge definitions and the Lo and m limits), ¶II-2.3.1.2 (vent pipe forces and blowback), ¶II-4.1 (loading criteria); ¶101.5.5 (discharge reactions) and ¶107.8.4 (reference to the Appendix) in the body of the Code.

SAMPLE REPORT — auto-generated from a verification fixture to show the report format. Not a project calculation. ⚠ Engineering-aid tool. Public code equations; allowable-stress and factor data are user-supplied. Results MUST be independently verified and reviewed by a qualified/licensed engineer before any design, fabrication, or operation decision.