WEIGHT & SPAN
Pipe
Medium
Insulation

Support Span
Results
Pipe linear mass
kg/m
Medium linear mass
kg/m
Insulation linear mass
kg/m
Total linear mass
kg/m
Section mass
kg
Paint area / linear
m²/m
Paint area (section)
Inside diameter ID
mm
Max span — simply supported
m
Max span — continuous supports
m
CROSS-SECTION
ODmmouter diameter
IDmminner diameter
smmwall thickness
Aflowcm²flow area
Ametalcm²metal cross-section
I×10⁻⁸ m⁴second moment of area
SIDE VIEW
L = — m OD —mm
Pressure Drop — Darcy-Weisbach
ε = 0.046 mm
m³/h
Pipeline segments
Results
ΔP total
kPa
ΔP total
bar
ΔP total (head)
m WC
Flow Parameters

m³/h
Recommended Velocity Ranges
Results
Cross-section
ID — mm
Velocity
— m/s 0 recommended
Flow velocity
m/s
Inside diameter
mm
Flow area
cm²
Mass flow
kg/h
PED 2014/68/EU — Category Classification
PED 2014/68/EU
Directive 2014/68/EU classifies pressure equipment into categories SEP / I–IV based on fluid hazard, pressure and size. Higher category = stricter conformity route.

Fluid Classification
PED Classification Result
SEP art.4(3) CAT I low CAT II medium CAT III high CAT IV critical
CE Marking
CE Marking
CE marking is mandatory for Cat I–IV. Equipment must bear CE mark + NB number (if applicable) before placing on EU market.
Conformity Route
Conformity Assessment
Module A: self-declaration. A2/D1/E1: supervised tests or QA. B+D/E/F: EC type exam + QA. G: unit verification. H/H1: full QA.
Notified Body
Notified Body (NB)
Third-party body accredited by member state. Required for Cat II (some modules), Cat III and IV.
Article / Table
Scope Check
PS × V or PS × DN
bar·L
SEP Threshold
PED 2014/68/EU Annex II — Tables 1–9 · Preliminary only
Pipe Wall Thickness
Standard
Pipe

Operating conditions

Material & factors
mm
%
Pipe Wall Thickness Result
t required
mm
t minimum (calc)
mm
Resulting ID
mm
Allowable stress S
MPa at T
P max (schedule)
bar
Schedule / Series comparison
Material

Pipe
DN — Anchor Force only
DN and wall thickness are used only for anchor force F = σ·A_wall. Thermal elongation ΔL is independent of pipe diameter.

Temperature Conditions
Thermal Expansion Result
Thermal Movement
ΔL expansion
ΔL at T_max
Free elongation T_inst → T_max. Positive = expansion.
mm
ΔL contraction
mm
Total range
Total movement range
ΔL_max − ΔL_min. Total displacement the expansion loop or flexible joint must absorb.
mm
Fully Restrained (worst case)
Thermal stress σ
Restrained thermal stress
σ = E·α·ΔT. Stress if pipe is fixed at both ends. Compare with material yield strength.
MPa
Anchor force F
Anchor force
F = σ·A_wall. Force on fixed anchor if pipe cannot expand. Based on selected DN and wall thickness.
kN
ΔL = α · L · ΔT | σ = E · α · ΔT | F = σ · A_wall · Preliminary only
NPSH Calculation
IN DEVELOPMENT
Available NPSHa vs required NPSHr. Cavitation margin assessment. Suction line sizing and recommendations to avoid cavitation.
Planned: Q3 2025
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Pump Working Point
IN DEVELOPMENT
System curve vs pump Q-H curve. Working point determination, parallel/series pump operation, affinity laws for speed adjustment.
Planned: Q3 2025
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Pump Power & Efficiency
IN DEVELOPMENT
Hydraulic power, shaft power, motor sizing. Efficiency curves, specific speed, impeller diameter estimation.
Planned: Q4 2025
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Heat Loss — Pipe Insulation
IN DEVELOPMENT
Steady-state heat loss through pipe wall and insulation layers. Multi-layer cylinder model. Economic insulation thickness, condensation risk on cold pipes.
Planned: Q3 2025
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💧
Steam Condensate & Trap Sizing
IN DEVELOPMENT
Condensate load from pipe warm-up and steady-state operation. Steam trap sizing and selection guidance.
Planned: Q4 2025
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Vessel Wall Thickness
IN DEVELOPMENT
Cylindrical shell and end cap thickness per ASME VIII Div.1 and EN 13445. Design pressure, temperature, material, weld joint efficiency.
Planned: Q4 2025
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Vessel Weight & Volume
IN DEVELOPMENT
Complete vessel mass breakdown — shell, heads, nozzles, internals, contents. Hydrostatic test weight. Centre of gravity.
Planned: Q4 2025
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Pipeline Volume Inventory
IN DEVELOPMENT
Build a pipeline system section by section. Add pipe lengths, fittings, valves, vessels — each with its bore volume. Total volume for hydrotesting, chemical dosing, filling time.
Planned: Q1 2026
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Gas Pressure Regulator

Upstream (1)

Downstream (2)

Flow & Valve
Results
Thermodynamic state
T₂ after throttling
°C
ΔT Joule-Thomson
K
Density ρ₁
kg/m³
Density ρ₂
kg/m³
Velocities
v₁ upstream
m/s
v₂ downstream
m/s
Choked flow check (ISA S75 / IEC 60534)
Critical p-ratio rcrit
Actual p-ratio ract
Flow regime
Choked Δp limit
bar
Valve sizing (IEC 60534)
Kv required
m³/h
Cv required
USgpm/psi⁰·⁵
Kv utilisation
%
Sizing basis
Tank Breathing — API 2000 / ISO 28300

Operational breathing

Thermal conditions

Tank limits & vent
Results — API 2000 6th Ed.
Thermal breathing(daily temperature cycle)
Inbreathing (vacuum)
Nm³/h
Outbreathing (pressure)
Nm³/h
Operational breathing (fill / empty)
Inbreathing (emptying)
Nm³/h
Outbreathing (filling)
Nm³/h
Design total(thermal + operational combined)
Total inbreathing
Nm³/h
Total outbreathing
Nm³/h
Vent sizing(at tank pressure limit)
Vent area (inbreathing)
cm²
Vent area (outbreathing)
cm²
Min vent DN (inbreathing)
DN
Min vent DN (outbreathing)
DN
Pressure / vacuum check
Max pressure limit
Max vacuum limit
Water Hammer — Joukowsky

Fluid / medium

Flow conditions

Surge screening limits
Results
Wave propagation
Wave speed a
m/s
Wave period 2L/a
s
Pressure surge
Joukowsky Δp
bar
Max pressure p_max (abs)
bar
Closure type
Safe closure t_c
s
Cavitation check
Min pressure p_min (abs)
bar
Cavitation risk
Surge screening
Screening result
Expansion Loop Sizing

Temperature & pipe run
Expansion Loop Results
Thermal expansion
Total ΔL
mm
ΔT
°C
Loop dimensions
Loop leg H
mm
Loop width W
mm
Pipe flexibility K
Stress ratio
%
Two-Phase Flow Regime

Gas phase

Liquid phase
Flow Regime — Baker / Mandhane
FLOW REGIME
Superficial velocities
v_SG (gas)
m/s
v_SL (liquid)
m/s
Void fraction α
Gas quality x
Slugging risk
Froude Fr
Slug risk
Support Configuration

Anchor Plate & Bolts

Applied Forces
Position a [mm from left/wall] Force F [kN]
Diagram — dimensions & load positions
Bending moment diagram
Results
Max moment M
kNm
Required Wel
cm³
Max shear V
kN
Deflection limit
mm
Recommended Profiles
Anchor Plate & Bolts — Results
Bolt shear force
kN/bolt
Bolt tension (moment)
kN/bolt
Min bolts required
pcs
Plate bending check