RFQ Assistant
Vendor-ready equipment datasheets, drafted from your P&ID with provenance per cell.
Pick an equipment tag from the P&ID. The system generates a structured datasheet for that piece of equipment, every row sourced as extracted, inferred, standard, or TBD. Engineers verify and overwrite, then issue to vendors.
Header
Project
Reactor & Product Separation (DDE-20-01)
HIGHHeader
Tag
R-201
HIGHHeader
Service
Catalytic ammonia synthesis (3 H2 + N2 → 2 NH3), promoted-iron catalyst, high-pressure / high-temperature hydrogen service
HIGHHeader
Quantity
1 ea
HIGHHeader
Location
—
LOWType & arrangement
Vessel type
Fixed-bed catalytic reactor — multi-bed ammonia synthesis converter (cold-shell, axial-radial flow with inter-bed quench and internal feed/effluent exchanger)
HIGHType & arrangement
Orientation
Vertical
HIGHType & arrangement
Head type
2:1 elliptical (ASME)
HIGHProcess conditions
Fluid
Synthesis gas (H2 + N2 + recycle inerts) reacting to NH3 over promoted-iron catalyst
HIGHProcess conditions
Operating pressure
≈ 145–149 barg
HIGHProcess conditions
Operating temperature
≈ 400 (inlet) / 430 (peak/outlet) °C
HIGHProcess conditions
Design pressure
165 barg
HIGHProcess conditions
Design temperature
470 °C
MEDIUMProcess conditions
MAWP
165 barg
HIGHProcess conditions
Specific gravity
—
LOWGeometry
Inside diameter
—
LOWGeometry
Tan-to-tan length
—
LOWGeometry
Shell thickness
—
LOWGeometry
Head thickness
—
LOWGeometry
Corrosion allowance
3.0 mm
MEDIUMInternals
Internals type
Three axial-radial flow catalyst baskets (promoted-iron NH3 synthesis catalyst), inter-bed quench gas distribution rings, internal feed/effluent heat exchanger between bed-3 outlet and bed-1 inlet, cold-shell internal liner isolating pressure shell from catalyst-bed temperatures
HIGHInternals
Demister / mesh pad
Not applicable
HIGHInternals
Instrument bridle
Not required — temperatures monitored by multi-point thermowells (TT-2032 in bed 1, TT-2033 across beds 2 and 3); pressure by top-nozzle PT-2031. No level service.
HIGHMaterials
Shell material
SA-336 F22V (2.25Cr-1Mo-0.25V) forged shell course, vacuum-degassed, weld-overlayed internally with austenitic stainless (typ. 309L+347)
MEDIUMMaterials
Head material
SA-336 F22V (matching shell), with internal stainless weld overlay
MEDIUMMaterials
Internals material
Catalyst basket / inter-bed exchanger tubes: SS 321H or Alloy 800H (high-T creep + nitriding resistance); distributor / quench rings: SS 321H
MEDIUMNozzles
Inlet nozzle
10 inch, top dome — preheated synthesis feed from E-201
HIGHNozzles
Outlet nozzle
12 inch, bottom — hot effluent to E-201 shell
HIGHNozzles
Relief / vent nozzle
PSV-2035 nozzle on top dome, discharging via 3"-FL-2035-A1B to HP flare header FH-001 (PSV set 165 barg)
HIGHNozzles
↳ Feed inlet (N1) · Service
Preheated synthesis feed in (top)
HIGHNozzles
↳ Feed inlet (N1) · Size · rating
10 inch · ASME B16.5 Class 1500 RTJ
HIGHNozzles
↳ Effluent outlet (N2) · Service
Hot reactor effluent out (bottom)
HIGHNozzles
↳ Effluent outlet (N2) · Size · rating
12 inch · ASME B16.5 Class 1500 RTJ
HIGHNozzles
↳ Quench gas inlet (N3 — manifolded to inter-bed rings) · Service
Cold quench gas to inter-bed distribution rings (between beds 1–2 and 2–3) under FCV-2034
HIGHNozzles
↳ Quench gas inlet (N3 — manifolded to inter-bed rings) · Size · rating
4 inch · ASME B16.5 Class 1500 RTJ
HIGHNozzles
↳ Relief nozzle (N4 — PSV-2035) · Service
PSV-2035 inlet on top dome to HP flare
HIGHNozzles
↳ Relief nozzle (N4 — PSV-2035) · Size · rating
Inlet ≥3 inch · ASME B16.5 Class 1500 RTJ (sized per API 520 — final by relief calc)
MEDIUMNozzles
↳ Pressure tap (N5 — PT-2031) · Service
Pressure transmitter PT-2031, top inlet (upstream of bed 1)
HIGHNozzles
↳ Pressure tap (N5 — PT-2031) · Size · rating
1.5 inch · ASME B16.5 Class 1500 RTJ
MEDIUMNozzles
↳ Thermowell nozzles (N6 — TT-2032 / TT-2033) · Service
Multi-point thermowells: TT-2032 (3-pt across bed 1) and TT-2033 (6-pt across beds 2 and 3) for catalyst hotspot monitoring
HIGHNozzles
↳ Thermowell nozzles (N6 — TT-2032 / TT-2033) · Size · rating
2 inch · ASME B16.5 Class 1500 RTJ (one nozzle per multi-point well)
MEDIUMNozzles
↳ Catalyst loading manway (N7) · Service
Top catalyst loading manway / handhole
MEDIUMNozzles
↳ Catalyst loading manway (N7) · Size · rating
≥18 inch blind · ASME B16.5 Class 1500 RTJ (final by vendor)
LOWNozzles
↳ Catalyst unloading nozzle (N8) · Service
Bottom catalyst unloading / drain
MEDIUMNozzles
↳ Catalyst unloading nozzle (N8) · Size · rating
≥6 inch blind · ASME B16.5 Class 1500 RTJ (final by vendor)
LOWCodes & standards
Design code
ASME VIII Div 2 Class 2 (latest edition), with HTHA assessment per API RP 941 Nelson curves
HIGHCodes & standards
NACE compliance
NACE MR0175 / ISO 15156 compliant for any portion that may see wet H2S during start-up, shutdown, or upset (recycle gas may carry traces)
HIGHCodes & standards
PWHT requirement
Mandatory — full PWHT per ASME VIII Div 2 §6.4.2 / ASME VIII §UCS-56 for 2.25Cr-1Mo-V (P-No 5A); also required by NACE MR0175 §7.2.1.2 for hardness control
HIGHTesting
Hydrostatic test
Shop hydrotest at 1.43 × MAWP corrected for temperature per ASME VIII Div 2 §8.2 (≈ 236 barg at ambient — final by vendor stress check)
HIGHTesting
RT / UT
100% volumetric examination of all pressure-retaining welds (RT or UT) per ASME VIII Div 2 §7.4 (Examination Group 1 / Joint Efficiency 1.0); plus 100% PT/MT of all weld-overlay surfaces
HIGHTesting
PMI / hardness
100% PMI on all alloy components and weld overlays; weld and HAZ hardness ≤ 22 HRC (235 HV) per NACE MR0175 §7.2.1; production test coupons per ASME VIII Div 2 §3.11 for Cr-Mo-V toughness/creep verification
HIGHCommercial
Delivery
—
LOWCommercial
Warranty
—
LOWCommercial
Scope of supply
—
LOW
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