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neqsim-hydrogen-production

Name: Neqsim Hydrogen Production
Author: equinor

// Hydrogen production routes (SMR/ATR/POX, blue-H2 WGS/capture/compression chains, electrolysis, ammonia cracking) with NeqSim. USE WHEN: modeling fired SMR reformers, ATR and POX syngas generators, water-gas shift, pressure-swing adsorption (PSA), CO2 capture/compression/export placeholders, H2 drying/compression/export, water electrolyzers (PEM/Alkaline/SOEC/AEM), stack I-V curves, hydrogen plant cost estimation, para/ortho hydrogen conversion, catalyst deactivation, or blue/green H2 flowsheets. Covers ReformerFurnace, CatalyticTubeReformer, WaterGasShiftReactor, ComponentCaptureUnit, BlueHydrogenPlantBuilder, AutothermalReformer, PartialOxidationReactor, PSACascade, Electrolyzer, ParaOrthoH2Correction, CatalystDeactivationKinetics, and cost estimates.

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updated:2026年5月28日 12:16

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同仓库

neqsim-dynamic-simulation.md

from "equinor/neqsim"

Dynamic simulation guidance for NeqSim. USE WHEN: running transient simulations, modeling startup/shutdown, tuning PID controllers, analyzing pressure/level dynamics, performing blowdown/depressurization, or setting up measurement devices and control loops. Covers runTransient, DynamicProcessHelper, controller tuning, and dynamic equipment configuration.

2026-05-30117

neqsim-power-generation.md

from "equinor/neqsim"

Power generation patterns for NeqSim. USE WHEN: modeling gas turbines, steam turbines, HRSG, combined cycle systems, waste heat recovery, or calculating fuel gas consumption and thermal efficiency. Covers GasTurbine, SteamTurbine, HRSG, CombinedCycleSystem classes and heat integration with PinchAnalysis.

2026-05-29117

neqsim-distillation-design.md

from "equinor/neqsim"

Distillation column design rules for NeqSim. USE WHEN: setting up distillation columns, troubleshooting convergence, selecting internals (trays/packing), sizing columns, or analyzing column performance. Covers DistillationColumn setup, solver selection, feed tray optimization, reflux ratio, and internals selection per industry standards.

2026-05-18117

neqsim-capability-map.md

from "equinor/neqsim"

Structured inventory of NeqSim's capabilities by engineering discipline. USE WHEN: checking what NeqSim can do, planning implementations, assessing gaps for engineering tasks, or routing work to the right agent. Covers thermodynamics, process equipment, PVT, standards, mechanical design, flow assurance, safety, and economics.

2026-05-10117

neqsim-controllability-operability.md

from "equinor/neqsim"

Process controllability and operability — operating envelope mapping, turndown analysis, startup/shutdown sequencing, control valve sizing per ISA-75 (Fl, Fp, choked flow), rangeability, hunting/loop tuning, recycle stability. USE WHEN: a task involves operability assessment, turndown studies, control valve sizing, startup/shutdown procedures, or 'will this design operate?' questions. Complements neqsim-dynamic-simulation (transient solver) with steady-state operability framing.

2026-05-10117

neqsim-depressurization-mdmt.md

from "equinor/neqsim"

Emergency depressurization (blowdown) per API 521 §5.20 and minimum design metal temperature (MDMT) assessment per ASME UCS-66 / API 579 / EN 13445 — VU-flash transient inventory model, time-to-target-pressure, low-temperature embrittlement screening, and integration with PSV/flare loads. USE WHEN: a task requires sizing a blowdown valve, generating a P-vs-time curve for a vessel under fire / depressurization, checking MDMT against blowdown end-temperature, providing source terms for relief and flare networks, or distinguishing blowdown from trapped-liquid fire rupture screening. Anchors on neqsim.process.safety.depressurization.DepressurizationSimulator and neqsim.process.safety.mdmt.MDMTCalculator.

2026-05-10117

package.json

"author": "equinor"

"repository": "equinor/neqsim"

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在 Manus 中运行

$ useful --forSOC

软件开发工程师计算机与数学类职业15-1252L4

name	neqsim-hydrogen-production
description	Hydrogen production routes (SMR/ATR/POX, blue-H2 WGS/capture/compression chains, electrolysis, ammonia cracking) with NeqSim. USE WHEN: modeling fired SMR reformers, ATR and POX syngas generators, water-gas shift, pressure-swing adsorption (PSA), CO2 capture/compression/export placeholders, H2 drying/compression/export, water electrolyzers (PEM/Alkaline/SOEC/AEM), stack I-V curves, hydrogen plant cost estimation, para/ortho hydrogen conversion, catalyst deactivation, or blue/green H2 flowsheets. Covers ReformerFurnace, CatalyticTubeReformer, WaterGasShiftReactor, ComponentCaptureUnit, BlueHydrogenPlantBuilder, AutothermalReformer, PartialOxidationReactor, PSACascade, Electrolyzer, ParaOrthoH2Correction, CatalystDeactivationKinetics, and cost estimates.
last_verified	2026-05-27

Hydrogen Production with NeqSim

Guide for modeling hydrogen production routes — steam methane reforming (SMR), autothermal reforming (ATR), partial oxidation (POX), PSA purification (blue H2), and water electrolysis (green/pink H2). Companion to neqsim-ccs-hydrogen (transport/storage/blending) and neqsim-reaction-engineering (reformer kinetics).

When to Use This Skill

SMR fired reformer, ATR, and POX plant flowsheets with WGS + PSA
Oxygen-to-carbon and steam-to-carbon envelope screening
Reformer furnace heat-balance and tube-wall checks
POX/ATR quench, refractory, soot-risk, and H2/CO screening
PSA bed sizing and purity/recovery analysis
Electrolyzer technology selection (PEM vs Alkaline vs SOEC vs AEM)
Stack voltage modeling from current density (I-V curves)
Specific energy consumption (kWh/kg H₂)
Hydrogen plant CAPEX estimation
Cryogenic para/ortho H₂ conversion screening
Catalyst activity decay for SMR/WGS/ammonia cracking studies
Blue vs green H₂ techno-economic comparison

Applicable Standards

Standard	Scope
ISO 14687	Hydrogen fuel quality (PEM-FC grade ≥ 99.97% H₂)
ISO 22734	Industrial water electrolyzers — safety
IEC 62282	Fuel cell technologies (electrochemistry conventions)
API 941	Steels for H₂ service (Nelson curves)
ASME B31.12	Hydrogen piping and pipelines
EIGA Doc 121	H₂ generator design (SMR/electrolysis)
IRENA 2022	Green H₂ cost benchmarks
IEA Global H₂ Review 2023	Capacity factors, USD/kW benchmarks

Core Classes (Thermochemical route templates)

Class	Package	Purpose
`CatalyticTubeReformer`	`neqsim.process.equipment.reactor`	Tube-side SMR equilibrium model with duty, pressure-drop, tube-wall, heat-flux, and catalyst-activity screening
`ReformerFurnace`	`neqsim.process.equipment.reactor`	Fired SMR furnace coupling `FurnaceBurner` combustion heat to reformer-tube duty
`SyngasBurnerZone`	`neqsim.process.equipment.reactor`	Oxygen-blown ATR/POX burner-zone model with O2/C envelope and flame-temperature screening
`AutothermalReformer`	`neqsim.process.equipment.reactor`	ATR template with O2/C and S/C controls, burner zone, catalytic equilibrium zone, and soot-risk metric
`PartialOxidationReactor`	`neqsim.process.equipment.reactor`	POX template with O2/C control, refractory warning, fast quench, and H2/CO output
`QuenchSection`	`neqsim.process.equipment.reactor`	Rapid syngas cooling model with heat-removed and quench-severity outputs
`WaterGasShiftReactor`	`neqsim.process.equipment.reactor`	HT/LT WGS equilibrium wrapper with CO conversion, H2 gain, CO2 formation, duty, and WGS ratio reporting
`ComponentCaptureUnit`	`neqsim.process.equipment.splitter`	Selective component-capture placeholder for CO2 capture, H2 drying, and other screening separations
`SMRHydrogenPlantBuilder`	`neqsim.process.hydrogen`	Screening plant builder for methane/steam feed, fired reformer, and optional PSA
`ATRHydrogenPlantBuilder`	`neqsim.process.hydrogen`	Screening plant builder for methane/steam/oxygen feed, ATR, and optional PSA
`POXHydrogenPlantBuilder`	`neqsim.process.hydrogen`	Screening plant builder for POX syngas or hydrogen studies with optional PSA
`BlueHydrogenPlantBuilder`	`neqsim.process.hydrogen`	Full screening chain for SMR + HT/LT WGS + CO2 capture/compression + PSA + H2 drying/compression + carbon intensity

Thermochemical maturity map

Technology	Implemented NeqSim pattern	Maturity	Remaining high-fidelity scope
Steam methane reforming (SMR)	`ReformerFurnace` + `CatalyticTubeReformer` + `FurnaceBurner`	4/5	Detailed radiant-box view factors, burner CFD, tube metallurgy/vendor rating
Autothermal reforming (ATR)	`AutothermalReformer` with `SyngasBurnerZone` + catalytic `GibbsReactor`	4/5	Burner aerodynamics, oxygen-mixing CFD, rate-based catalyst bed calibration
Partial oxidation (POX)	`PartialOxidationReactor` + `SyngasBurnerZone` + `QuenchSection`	3/5	Fast-quench kinetics, refractory thermal model, soot/coke kinetics

Core Classes (Horizon 1)

Class	Package	Purpose
`PressureSwingAdsorptionBed`	`neqsim.process.equipment.adsorber`	H₂-tuned single PSA bed (AC or Zeolite 13X)
`AdsorptionCycleController`	`neqsim.process.equipment.adsorber`	Multi-bed Skarstrom-style cycling (pre-existing)
`Electrolyzer`	`neqsim.process.equipment.electrolyzer`	Stack model with technology defaults and Faradaic efficiency
`ElectrolyzerTechnology`	same	Enum PEM / ALKALINE / SOEC / AEM with default voltage, current density, T, P, η_F
`ElectrolyzerIVCharacteristic`	same	Tafel + ohmic voltage model; tech-specific defaults
`ElectrolyzerCostEstimate`	`neqsim.process.costestimation.electrolyzer`	Specific-CAPEX × scale-factor × CEPCI

Core Classes (Horizon 1.5)

Class	Package	Purpose
`PSACascade`	`neqsim.process.equipment.adsorber`	Multi-bed Skarstrom cascade (2/4/6/8/10/12 beds) with recovery uplift from pressure equalisation
`PSACostEstimate`	`neqsim.process.costestimation.adsorber`	Per-bed vessel + valve skid + sorbent inventory × CEPCI

Core Classes (Horizon 3 foundations)

Class	Package	Purpose
`ParaOrthoH2Correction`	`neqsim.thermo.util.hydrogen`	Equilibrium para fraction, normal-to-equilibrium heat release, Cp correction, thermal-conductivity factor, conversion time
`CatalystDeactivationKinetics`	`neqsim.process.equipment.reactor`	First-order activity decay for sulfur/chloride poisoning, coking, and thermal sintering

Recipe 0 — SMR / ATR / POX route builders

Use the route builders when a task needs a runnable screening flowsheet quickly. They create feeds with correct trace syngas products, set SRK + classic mixing, wire the reactor model, and optionally add a PSA cascade.

ProcessSystem smr = new SMRHydrogenPlantBuilder().setName("SMR screening")
    .setMethaneFeedMolePerSec(100.0)
    .setSteamToCarbonRatio(3.0)
    .setIncludePsa(true)
    .build();
smr.run();

ReformerFurnace furnace =
    (ReformerFurnace) smr.getUnit("SMR screening reformer furnace");
double dutyKW = furnace.getTubeHeatDemandKW();
double heatBalance = furnace.getHeatBalanceRatio();

ProcessSystem atr = new ATRHydrogenPlantBuilder().setName("ATR screening")
    .setMethaneFeedMolePerSec(100.0)
    .setSteamToCarbonRatio(1.5)
    .setOxygenToCarbonRatio(0.60)
    .setIncludePsa(true)
    .build();
atr.run();

ProcessSystem pox = new POXHydrogenPlantBuilder().setName("POX screening")
    .setMethaneFeedMolePerSec(100.0)
    .setOxygenToCarbonRatio(0.55)
    .setSteamToCarbonRatio(0.20)
    .build();
pox.run();

Key route outputs:

ReformerFurnace: getSyngasOutStream(), getFlueGasOutStream(), getTubeHeatDemandKW(), getAvailableRadiantHeatKW(), getHeatBalanceRatio().
CatalyticTubeReformer: getMethaneConversion(), getHeatDuty("kW"), getTubeWallTemperature(), isTubeWallTemperatureAcceptable().
AutothermalReformer: getOxygenToCarbonRatio(), getSteamToCarbonRatio(), getMethaneConversion(), getSootRiskIndex(), getBurnerZone().
PartialOxidationReactor: getHydrogenToCarbonMonoxideRatio(), getRefractoryWarning(), getQuenchSection(), getSootRiskIndex().
Every new route unit exposes getResults() and toJson() for agent reports.

Recipe 1 — Blue H₂ full chain (SMR + WGS + capture + PSA + export)

BlueHydrogenPlantBuilder builder = new BlueHydrogenPlantBuilder()
    .setName("Blue H2 screening")
    .setMethaneFeedMolePerSec(100.0)
    .setSteamToCarbonRatio(3.0)
    .setCo2CaptureFraction(0.90)
    .setCo2ExportPressure(110.0)
    .setH2ExportPressure(100.0)
    .setIncludePsa(true);

ProcessSystem process = builder.build();
process.run();

double h2KgPerHr = builder.getHydrogenProductMassFlowKgPerHour();
double capturedCo2KgPerHr = builder.getCapturedCo2MassFlowKgPerHour();
double residualIntensity = builder.getCarbonIntensityKgCO2PerKgH2();
double grossIntensity = builder.getGrossCarbonIntensityKgCO2PerKgH2();
String resultsJson = builder.toJson();

Notes

The default sequence is SMR furnace → HT WGS → LT WGS → cooler/KO → CO2 capture → CO2 compressor → PSA → H2 dryer → H2 compressor.
WaterGasShiftReactor treats methane, nitrogen, and oxygen as inert and reports CO conversion, H2 gain, CO2 formation, heat duty, and WGS ratio.
ComponentCaptureUnit is a screening placeholder. Use it for CO2 capture and H2 drying when detailed amine, membrane, or molecular-sieve packages are not yet available.
Carbon-intensity reporting counts residual direct carbon as CO2 equivalent and reports both residual and gross intensity per kg H2 product.

Recipe 1b — PSA-only purification block

PressureSwingAdsorptionBed psa = new PressureSwingAdsorptionBed("PSA", koVap);
psa.setSorbent(PressureSwingAdsorptionBed.SorbentType.ACTIVATED_CARBON);
psa.setRecoveryTarget(0.88);
psa.run();

double purityH2 = psa.getH2Purity();
double recoveryH2 = psa.getH2Recovery();
double[] tailComp = psa.getTailGasComposition();

Use the standalone PSA block when a shifted syngas stream is already available from a custom flowsheet.

Recipe 2 — Green H₂ Electrolyzer

// Water feed to the stack — molar flow sets the H₂ production target.
SystemInterface water = new Fluid().create("water");
Stream feed = new Stream("water", water);
feed.setFlowRate(100.0, "mole/sec");      // ~10 kg H₂/hr at η_F = 1
feed.setTemperature(298.15, "K");
feed.setPressure(1.0, "bara");
feed.run();

Electrolyzer el = new Electrolyzer("PEM stack", feed);
el.setTechnology(ElectrolyzerTechnology.PEM);  // applies V/j/T/P/η_F defaults
el.setIVCharacteristic(new ElectrolyzerIVCharacteristic(ElectrolyzerTechnology.PEM));
el.run();

double power_kW = el.getStackPower();
double sec      = el.getSpecificEnergyConsumption_kWh_per_kg_H2();
double V_cell   = el.getCellVoltage();   // recomputed from I-V at run time

Technology selector

Tech	V_cell	j (A/cm²)	T (°C)	P (bara)	η_F	Specific energy (kWh/kg)
PEM	1.80	2.0	80	30	0.65	~45–55
ALKALINE	1.85	0.4	80	7	0.62	~50–60
SOEC	1.30	1.0	800	1	0.85	~35–40 (HHV)
AEM	1.85	0.8	60	10	0.60	~55–65

Sources: IRENA 2022 Hydrogen Decarbonisation Pathways; Buttler & Spliethoff RSER 82 (2018); IEA Global H₂ Review 2023.

I-V curve internals

getCellVoltage(j, T_K) = E_rev(T) + A · log10(j / j0) + R · j

E_rev(T) = 1.229 V + (-0.85 mV/K) · (T - 298.15) (Larminie & Dicks)
Tafel slope A, exchange current j0, ASR R are technology defaults
Below j0 the model returns E_rev (no spurious negative overpotential)

Recipe 4 — Multi-bed PSA cascade

PSACascade cascade = new PSACascade("H2-PSA", koVap);
cascade.setConfiguration(PSACascade.CascadeConfiguration.BEDS_6);  // 6 beds, 2 PEQ
cascade.setSorbent(PressureSwingAdsorptionBed.SorbentType.ACTIVATED_CARBON);
cascade.setPerBedRecoveryTarget(0.82);   // single-bed equilibrium recovery
cascade.setCycleTime(300.0);             // seconds per bed cycle
cascade.run();

double purity   = cascade.getH2Purity();        // > 99.9 %
double recovery = cascade.getH2Recovery();      // single-bed + cascade uplift
Stream tail     = cascade.getTailGasStream();   // for SMR fuel-gas balance

Cascade uplift table (pressure equalisation steps → recovery gain over a single bed):

Configuration	Beds	Equalisations	Uplift
`BEDS_2`	2	0	+0.00
`BEDS_4`	4	1	+0.05
`BEDS_6`	6	2	+0.08
`BEDS_8`	8	3	+0.10
`BEDS_10`	10	4	+0.11
`BEDS_12`	12	5	+0.12

Total cascade recovery is capped at 0.93 (industrial benchmark for H₂ PSA on shifted syngas).

Recipe 5 — PSA cascade CAPEX

PSACostEstimate cost = new PSACostEstimate(cascade);   // derives N_beds, sorbent, mass
cost.calculateCostEstimate();
double usd = cost.getPurchasedEquipmentCost();

Reference per-bed vessel cost: USD 250 000 at 2 m × 4 m TL-TL, scale exponent 0.6.
Valve skid: USD 60 000 per bed (manifold + actuators + cycle controller).
Sorbent inventory: USD 4/kg AC or USD 10/kg Zeolite 13X.
Balance-of-plant strip (setIncludeBalanceOfPlant(false)) removes ~25 % for vessel-only quotes.
CEPCI 2024 = 800 reference; multiply by CostEstimationCalculator.getCurrentCepci()/800.

Recipe 6 — Para/ortho H₂ correction for cryogenic screening

double para20K = ParaOrthoH2Correction.getEquilibriumParaFraction(20.0);
double heatJPerKg = ParaOrthoH2Correction.getNormalToEquilibriumHeatJPerKg(20.0);
double cpCorrection = ParaOrthoH2Correction.getCpCorrectionJPerKgK(40.0);
double conductivityFactor = ParaOrthoH2Correction.getThermalConductivityCorrectionFactor(20.0);
double tauSeconds = ParaOrthoH2Correction.estimateEquilibrationTimeSeconds(
    77.0, ParaOrthoH2Correction.ConversionCatalyst.HYDROUS_FERRIC_OXIDE);

Normal hydrogen is 25% para; equilibrium hydrogen approaches >99% para near 20 K.
getNormalToEquilibriumHeatJPerKg(T) returns positive exothermic heat release.
getCpCorrectionJPerKgK(T) is equilibrium minus frozen-normal rotational heat capacity.
Thermal-conductivity correction factors are bounded screening multipliers for normal-H₂ correlations.

Recipe 7 — Catalyst deactivation activity factor

CatalystBed bed = new CatalystBed();
CatalystDeactivationKinetics kinetics = new CatalystDeactivationKinetics(
    CatalystDeactivationKinetics.CatalystFamily.NICKEL_REFORMING)
        .setTemperature(973.15)
        .setSulfurPpmv(0.05)
        .setCarbonPotential(0.5)
        .setSteamToCarbonRatio(2.5)
        .setOperationHours(8000.0);

double activity = kinetics.applyTo(bed);
double timeTo80 = kinetics.estimateTimeToActivity(0.80);
String mechanism = kinetics.getDominantMechanism();

Families: NICKEL_REFORMING, IRON_CHROMIUM_HT_SHIFT, COPPER_ZINC_LT_SHIFT, RUTHENIUM_AMMONIA_CRACKING.
Mechanisms: sulfur poisoning, chloride poisoning, coking, and thermal sintering.
Use vendor/lab/historian coefficients before detailed run-length guarantees.

Recipe 3 — Electrolyzer CAPEX

el.initMechanicalDesign();
ElectrolyzerMechanicalDesign mech =
    (ElectrolyzerMechanicalDesign) el.getMechanicalDesign();
mech.calcDesign();   // populates totalPowerKW

ElectrolyzerCostEstimate cost = new ElectrolyzerCostEstimate(mech);
cost.setTechnology("PEM");
double usd = cost.getPurchasedEquipmentCost();

Specific CAPEX (2024 USD/kW, CEPCI 800): PEM 1250, Alkaline 800, SOEC 2500, AEM 1500.
Scale exponent 0.85 vs reference 1 MW.
setIncludeBalanceOfPlant(false) strips ~35% for stack-only quotes.
Numbers are AACE Class 4–5 — do not use for FID without vendor budget quotes.

Color taxonomy and route map

Color	Route	NeqSim primitives
Grey	SMR no CCS	GibbsReactor + WGS + `PressureSwingAdsorptionBed`
Blue	SMR/ATR + CCS	Add CO₂ capture (amine/MEA) → see `neqsim-ccs-hydrogen`
Green	Renewable electrolysis	`Electrolyzer` with PEM/Alkaline + renewable power feed
Pink	Nuclear electrolysis	Same `Electrolyzer`, accounting differs
Turquoise	Methane pyrolysis	Not yet — Horizon 2

Common pitfalls

Thermochemical scope: ReformerFurnace, AutothermalReformer, and PartialOxidationReactor are route-screening models, not vendor reactor designs. Use them for heat balance, O2/C and S/C envelopes, soot/refractory warnings, and handoff to WGS/PSA/CO2 capture. Use vendor data or detailed CFD for radiant-box, burner, and tube-rating guarantees.
Trace products: Gibbs syngas models need product components present in the feed. The route builders and HydrogenProductionUtils.ensureSyngasComponents() add hydrogen, CO, and CO2 at trace levels.
ATR/POX controls: ratio controls rebuild the controlled inlet clone from methane moles before running. Disable ratio control only when a measured or externally generated feed composition must be preserved exactly.
PressureSwingAdsorptionBed.run() mass balance: product purity is computed from feedH2 × recovery ÷ remaining light gases. Always set the recovery target before run(); default is 0.85.
Electrolyzer voltage: when no ElectrolyzerTechnology is set, the legacy fixed-voltage path (V = 1.23 V, η_F = 1.0) stays active for backward compatibility.
Specific energy: getSpecificEnergyConsumption_kWh_per_kg_H2() is stackPower_kW / (n_H2 · MW_H2 · 3600). Below ~33 kWh/kg means the model is predicting >100% LHV efficiency — recheck inputs.
Cost estimate: requires mech.calcDesign() before construction so totalPowerKW > 0.
Para/ortho scope: ParaOrthoH2Correction is a screening correction, not a complete liquefaction process model.
Catalyst life scope: CatalystDeactivationKinetics default coefficients are order-of-magnitude values. Tune them to vendor or historian data for plant-specific forecasts.

Tests for verification

Test	Coverage
`PressureSwingAdsorptionBedTest`	Defaults, recovery cap, mass balance, composition, sorbent switch
`PSACascadeTest`	Cascade uplift, bed-count monotonicity, 0.93 cap, tail-gas mass balance
`PSACostEstimateTest`	Bed-count linearity, sorbent ordering, BoP toggle, order of magnitude
`ParaOrthoH2CorrectionTest`	Para equilibrium limits, conversion heat, Cp correction, conductivity factor, catalyst time ranking
`CatalystDeactivationKineticsTest`	Catalyst-family sensitivity, coking, sintering, dominant mechanism, CatalystBed activity update
`ElectrolyzerTechnologyTest`	Per-tech default consistency
`ElectrolyzerIVCharacteristicTest`	E_rev vs T, Tafel monotonicity, technology ordering
`ElectrolyzerTest`	Backward compat + η_F + I-V + specific-energy band
`ElectrolyzerCostEstimateTest`	Per-tech ordering, BoP toggle, scale economy
`HydrogenProductionReactorTest`	SMR tube/furnace metrics, ATR ratio controls, POX quench/refractory metrics, equipment factory aliases
`HydrogenPlantBuilderTest`	Runnable SMR, ATR, POX, and blue-H2 plant builder templates

Deferred (Horizon 2/3)

Rate-based amine absorber for CO₂ capture upstream of blue H₂
Full cryogenic H₂ liquefaction train with expanders and heat integration
High-fidelity reformer radiant-box view factors, burner CFD, and vendor tube-rating integration
Ammonia cracking kinetics for H₂ delivery from NH₃
Hydrogen LCA per production step
LOHC and photo-electrolysis

neqsim-hydrogen-production

同仓库更多 Skills

同仓库更多 Skills

Hydrogen Production with NeqSim

When to Use This Skill

Applicable Standards

Core Classes (Thermochemical route templates)

Thermochemical maturity map

Core Classes (Horizon 1)

Core Classes (Horizon 1.5)

Core Classes (Horizon 3 foundations)

Recipe 0 — SMR / ATR / POX route builders

Recipe 1 — Blue H₂ full chain (SMR + WGS + capture + PSA + export)

Recipe 1b — PSA-only purification block

Recipe 2 — Green H₂ Electrolyzer

Recipe 4 — Multi-bed PSA cascade

Recipe 5 — PSA cascade CAPEX

Recipe 6 — Para/ortho H₂ correction for cryogenic screening

Recipe 7 — Catalyst deactivation activity factor

Recipe 3 — Electrolyzer CAPEX

Color taxonomy and route map

Common pitfalls

Tests for verification

Deferred (Horizon 2/3)

Hydrogen Production with NeqSim

When to Use This Skill

Applicable Standards

Core Classes (Thermochemical route templates)

Thermochemical maturity map

Core Classes (Horizon 1)

Core Classes (Horizon 1.5)

Core Classes (Horizon 3 foundations)

Recipe 0 — SMR / ATR / POX route builders

Recipe 1 — Blue H₂ full chain (SMR + WGS + capture + PSA + export)

Recipe 1b — PSA-only purification block

Recipe 2 — Green H₂ Electrolyzer

Recipe 4 — Multi-bed PSA cascade

Recipe 5 — PSA cascade CAPEX

Recipe 6 — Para/ortho H₂ correction for cryogenic screening

Recipe 7 — Catalyst deactivation activity factor

Recipe 3 — Electrolyzer CAPEX

Color taxonomy and route map

Common pitfalls

Tests for verification

Deferred (Horizon 2/3)