Combien d'outils expose com.engscript/mcp ?

com.engscript/mcp expose 60 outil(s). Le coût de contexte pour les charger tous est d'environ 27684 tokens (coût unique au chargement, pas par appel).

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com.engscript/mcp

serveur MCP (Model Context Protocol) · engscript 1.0.0

▸ Géo & Temps

[ Non encore testé ]

Verdict MCP Hub
Référencé dans l'annuaire. Seul le pentest comportemental fait foi, et il n'a pas encore été exécuté sur ce serveur.

streamable-httpType / transport

directAccès

~27684 tokensCoût de contexte

60Outils

Est-ce que com.engscript/mcp est sûr ?

Au dernier audit MCP Hub, le serveur MCP « com.engscript/mcp » est classé « Non encore testé ». Référencé dans l'annuaire. Seul le pentest comportemental fait foi, et il n'a pas encore été exécuté sur ce serveur. Le verdict est réévalué en continu ; consultez la fiche pour l'état à jour.

Méthode : MCP Hub analyse la description de chaque outil (couche 1) et, pour le verdict fort, exécute le serveur dans une micro-VM isolée avec leurres et réseau bloqué (couche 2). On publie des noms et des compteurs, jamais le contenu brut renvoyé par un outil.

Les 60 outils

BALANCE≈ 190 tokens
General mass/energy balance solver using GEKKO
Paramètres, retour & exemple (4)
Paramètres
- EQUATION · object · requis
  Equality/inequality constraints. Keys prefixed eq/ge/le/gt/lt. Each entry: {'left': expr, 'right': expr}.
- MAXIMIZE · object · optionnel
  Objective to maximize. Format: {'left': 'maxtarget', 'right': 'expr'}.
- MINIMIZE · object · optionnel
  Objective to minimize. Format: {'left': 'mintarget', 'right': 'expr'}.
- VARIABLE · object · requis
  Decision variables. Each entry: [lb, init, ub] for free variable, or [fixed, fixed, fixed] for constant.
Exemple d'appel
```
{"name": "BALANCE", "arguments": {"EQUATION": {}, "VARIABLE": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
CARBON≈ 753 tokens
Calculate thermodynamic properties of hydrocarbon mixture. Supports hydrocarbons and non-hydrocarbon chemicals (PR EOS flash calculation).
Paramètres, retour & exemple (11)
Paramètres
- P · object · requis
  Pressure
- T · object · requis
  Temperature
- HC · array · requis
  List of component formula strings. Supported: H2, CH4, C2H2, C2H4, C2H6, C3H4, C3H6, C3H8, C4H8, C4H10, C5H12, C6H14, C7H16, C8H18, C9H20, C10H22, C6H6, C7H8, C8H10, C5H12O, Air, Ar, N2, O2, CO, CO2, H2O, H2S, NH3, SO2, SO3, HCl, NO2, N2O, N2O4, NaOH, N2O4
- mole · array · requis
  Mole fraction list corresponding to HC, e.g. [0.85, 0.10, 0.03, 0.02]
- H_unit · string · optionnel · Btu/lb | Btu/lbm | J/g | J/kg | cal/g | cal/kg | kJ/g | kJ/kg
  Enthalpy unit
- S_unit · string · optionnel · Btu/lb-F | Btu/lb-R | Btu/lbm-F | Btu/lbm-R | J/g-C | J/g-K | J/kg-C | J/kg-K
  Entropy unit
- Cp_unit · string · optionnel · Btu/lb-F | Btu/lb-R | Btu/lbm-F | Btu/lbm-R | J/g-C | J/g-K | J/kg-C | J/kg-K
  Cp unit
- Cv_unit · string · optionnel · Btu/lb-F | Btu/lb-R | Btu/lbm-F | Btu/lbm-R | J/g-C | J/g-K | J/kg-C | J/kg-K
  Cv unit
- rho_unit · string · optionnel · API | SG_H2O4 | SG_H2O60api | SG_H2O60nbs | g/cm3 | g/cm^3 | kg/m3 | kg/m^3
  Density unit
- Tbub_unit · string · optionnel · C | F | K | R
  Bubble point temperature unit
- Tdew_unit · string · optionnel · C | F | K | R
  Dew point temperature unit
Exemple d'appel
```
{"name": "CARBON", "arguments": {"P": {}, "T": {}, "HC": [], "mole": []}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
COMPPOLYEFF≈ 430 tokens
Calculate polytropic efficiency of compressor
Paramètres, retour & exemple (5)
Paramètres
- k · object · requis
  Heat capacity ratio
- Pi · object · requis
  Inlet pressure
- Po · object · requis
  Outlet pressure
- Ti · object · requis
  Inlet temperature
- To · object · requis
  Outlet temperature
Exemple d'appel
```
{"name": "COMPPOLYEFF", "arguments": {"k": {}, "Pi": {}, "Po": {}, "Ti": {}, "To": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
CTWRCAPA≈ 117 tokens
Cooling tower capacity evaluation
Paramètres, retour & exemple (2)
Paramètres
- INPUT · object · requis
- OUTPUT · object · optionnel
Exemple d'appel
```
{"name": "CTWRCAPA", "arguments": {"INPUT": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
CTWRCAPADSNTST≈ 266 tokens
Cooling tower capacity evaluation: design vs test
Paramètres, retour & exemple (2)
Paramètres
- INPUT · object · requis
- OUTPUT · object · optionnel
Exemple d'appel
```
{"name": "CTWRCAPADSNTST", "arguments": {"INPUT": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
CTWREVAPOR≈ 111 tokens
Cooling tower evaporation rate: mass removal rate (MR) and heat removal rate (QR)
Paramètres, retour & exemple (2)
Paramètres
- INPUT · object · requis
- OUTPUT · object · optionnel
Exemple d'appel
```
{"name": "CTWREVAPOR", "arguments": {"INPUT": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
CTWRLG≈ 92 tokens
Cooling tower L/G ratio calculation
Paramètres, retour & exemple (2)
Paramètres
- INPUT · object · requis
- OUTPUT · object · optionnel
Exemple d'appel
```
{"name": "CTWRLG", "arguments": {"INPUT": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
CTWRNTU≈ 113 tokens
Cooling tower NTU and characteristic C value calculation
Paramètres, retour & exemple (2)
Paramètres
- INPUT · object · requis
- OUTPUT · object · optionnel
Exemple d'appel
```
{"name": "CTWRNTU", "arguments": {"INPUT": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
CVGAS≈ 567 tokens
Calculate gas control valve Cv and Kv from flow conditions
Paramètres, retour & exemple (8)
Paramètres
- Q · object · requis
  Gas volumetric flow rate at standard conditions
- k · object · requis
  Specific heat ratio (Cp/Cv)
- MW · object · requis
  Gas molecular weight
- P1 · object · requis
  Upstream pressure
- P2 · object · requis
  Downstream pressure
- T1 · object · requis
  Inlet gas temperature
- Cv_unit · string · optionnel ·
  Output Cv unit
- Kv_unit · string · optionnel ·
  Output Kv unit
Exemple d'appel
```
{"name": "CVGAS", "arguments": {"Q": {}, "k": {}, "MW": {}, "P1": {}, "P2": {}, "T1": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
CVLIQ≈ 814 tokens
Calculate liquid control valve Cv and Kv from flow conditions
Paramètres, retour & exemple (9)
Paramètres
- Q · object · requis
  Liquid volumetric flow rate
- FL · object · optionnel
  Liquid pressure recovery factor (optional, default 0.9)
- P1 · object · requis
  Upstream pressure
- P2 · object · requis
  Downstream pressure
- Pc · object · optionnel
  Liquid critical pressure (optional, default 22120 kPa)
- Pv · object · optionnel
  Liquid vapor pressure (optional, default 0 kPa)
- rho · object · requis
  Liquid density
- Cv_unit · string · optionnel ·
  Output Cv unit
- Kv_unit · string · optionnel ·
  Output Kv unit
Exemple d'appel
```
{"name": "CVLIQ", "arguments": {"Q": {}, "P1": {}, "P2": {}, "rho": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
CVSTEAM≈ 476 tokens
Calculate steam control valve Cv and Kv from flow conditions
Paramètres, retour & exemple (6)
Paramètres
- M · object · requis
  Steam mass flow rate
- P1 · object · requis
  Upstream pressure
- P2 · object · requis
  Downstream pressure
- rho · object · requis
  Steam density
- Cv_unit · string · optionnel ·
  Output Cv unit
- Kv_unit · string · optionnel ·
  Output Kv unit
Exemple d'appel
```
{"name": "CVSTEAM", "arguments": {"M": {}, "P1": {}, "P2": {}, "rho": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
DESUPERHEATER≈ 792 tokens
Calculate boiler feed water flow and total flow from pressure and temperature reduction through desuperheater. Also returns the inlet/outlet/BFW specific enthalpies (h_in, h_out, h_bfw) used in the mass balance, always in Btu/lb.
Paramètres, retour & exemple (9)
Paramètres
- Min · object · requis
  Inlet steam flow rate
- Pin · object · requis
  Inlet steam pressure
- Tin · object · requis
  Inlet steam temperature
- Pbfw · object · requis
  BFW (boiler feed water) pressure
- Pout · object · requis
  Outlet steam pressure
- Tbfw · object · requis
  BFW (boiler feed water) temperature
- Tout · object · requis
  Outlet steam temperature
- Mbfw_unit · string · optionnel · kg/day | kg/hr | kg/min | kg/sec | klb/hr | lb/day | lb/hr | ton/day
  Required BFW (boiler feed water) flow unit
- Mout_unit · string · optionnel · kg/day | kg/hr | kg/min | kg/sec | klb/hr | lb/day | lb/hr | ton/day
  Total output steam flow unit
Exemple d'appel
```
{"name": "DESUPERHEATER", "arguments": {"Min": {}, "Pin": {}, "Tin": {}, "Pbfw": {}, "Pout": {}, "Tbfw": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
DVR≈ 240 tokens
Data Validation and Reconciliation
Paramètres, retour & exemple (3)
Paramètres
- ACCURACY · object · requis
  Measurement accuracy in %. Format: {TAG: {value: number, unit: '%'}}. Example: {A: {value: 5, unit: '%'}}
- EQUATION · object · requis
  Constraint equations. Format: {EQ1: 'A=B+C', EQ2: 'C=D+E'}. Each value is an equation string with '=' separator.
- MEASURED · object · requis
  Measured values. Format: {TAG: {value: number, unit: string}}. Example: {A: {value: 100, unit: ''}}
Exemple d'appel
```
{"name": "DVR", "arguments": {"ACCURACY": {}, "EQUATION": {}, "MEASURED": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
ECONOMIC≈ 150 tokens
Economic analysis: NPV, IRR, Simple Payback, Profitability Index, EAC
Paramètres, retour & exemple (2)
Paramètres
- R · object · optionnel
  Discount rate (fraction, e.g. 0.1 for 10%). Default 0.1.
- CF · object · requis
  Cash flow list, period 0 (initial investment, negative) through final period, e.g. [-100000, 30000, 30000, 30000]
Exemple d'appel
```
{"name": "ECONOMIC", "arguments": {"CF": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
EMISSIONFACTOR≈ 162 tokens
Calculate CO2 emission conversion factor from gas composition
Paramètres, retour & exemple (3)
Paramètres
- HC · array · requis
  List of fuel component formula strings, e.g. ['CH4', 'C3H8', 'N2', 'CO2']
- mole · array · requis
  Mole fraction list corresponding to HC, e.g. [0.88, 0.05, 0.04, 0.03]
- ECF_unit · string · optionnel · CO2-g/MBtu | CO2-kg/MBtu | CO2-lb/MBtu | CO2-ton/MBtu
  Emission factor output unit
Exemple d'appel
```
{"name": "EMISSIONFACTOR", "arguments": {"HC": [], "mole": []}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
FLUEGAS≈ 380 tokens
Calculate enthalpy of flue gas from composition
Paramètres, retour & exemple (7)
Paramètres
- HC · array · requis
  List of fuel component formula strings, e.g. ['CH4', 'C2H6', 'N2']
- Tb · object · requis
  Base temperature
- Tg · object · requis
  Flue gas temperature
- mole · array · requis
  Mole fraction list corresponding to HC, e.g. [0.90, 0.05, 0.05]
- Cp_unit · string · optionnel · Btu/lb-F | Btu/lb-R | Btu/lbm-F | Btu/lbm-R | J/g-C | J/g-K | J/kg-C | J/kg-K
  Cp output unit
- MW_unit · string · optionnel · g/gmol | g/mol | kg/kgmol | kg/kmol | lb/lbmol | lb/mol
  MW output unit
- dH_unit · string · optionnel · Btu/lb | Btu/lbm | J/g | J/kg | cal/g | cal/kg | kJ/g | kJ/kg
  Enthalpy output unit
Exemple d'appel
```
{"name": "FLUEGAS", "arguments": {"HC": [], "Tb": {}, "Tg": {}, "mole": []}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
FORMULA≈ 79 tokens
Generic formula calculator with unit conversion and IF-THEN-ELSE
Paramètres, retour & exemple (4)
Paramètres
- UNIT · object · optionnel
- INPUT · object · requis
- OUTPUT · object · requis
- FORMULA · object · requis
Exemple d'appel
```
{"name": "FORMULA", "arguments": {"INPUT": {}, "OUTPUT": {}, "FORMULA": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
FUELGAS≈ 250 tokens
Calculate MW, LHV and HHV of fuel gas from composition
Paramètres, retour & exemple (5)
Paramètres
- HC · array · requis
  List of fuel component formula strings, e.g. ['CH4', 'C2H6', 'H2', 'N2']
- mole · array · requis
  Mole fraction list corresponding to HC, e.g. [0.90, 0.05, 0.03, 0.02]
- MW_unit · string · optionnel · g/gmol | g/mol | kg/kgmol | kg/kmol | lb/lbmol | lb/mol
  MW output unit
- HHV_unit · string · optionnel · Btu/lb | Btu/lbm | J/g | J/kg | cal/g | cal/kg | kJ/g | kJ/kg
  HHV output unit
- LHV_unit · string · optionnel · Btu/lb | Btu/lbm | J/g | J/kg | cal/g | cal/kg | kJ/g | kJ/kg
  LHV output unit
Exemple d'appel
```
{"name": "FUELGAS", "arguments": {"HC": [], "mole": []}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
GN2DEPRESS≈ 491 tokens
Calculate depressurization gas volume and hold time for gaseous nitrogen storage vessel
Paramètres, retour & exemple (6)
Paramètres
- P1 · object · requis
  Initial pressure
- P2 · object · requis
  Final pressure
- Q2 · object · requis
  Nitrogen consumption rate
- V1 · object · requis
  Vessel volume
- H_unit · string · optionnel · days | hours | minutes | seconds | years
  Required hold time unit
- V2_unit · string · optionnel · MSCF | Nm3 | SCF | Sm3 | kNm3 | kSCF | kSm3
  Available gas volume unit
Exemple d'appel
```
{"name": "GN2DEPRESS", "arguments": {"P1": {}, "P2": {}, "Q2": {}, "V1": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
HEXRF≈ 2784 tokens
Heat exchanger fouling resistance back-calculation from shell/tube-side operating conditions.
Paramètres, retour & exemple (41)
Paramètres
- F · object · requis
  Correction factor (dimensionless)
- A_hex · object · requis
  Total heat transfer area
- k_hex · object · requis
  Tube wall thermal conductivity
- D_shll · object · requis
  Shell inside diameter
- D_tube · object · requis
  Tube outside diameter
- D_wall · object · requis
  Tube wall thickness
- L_tube · object · requis
  Tube length
- N_tube · object · requis
  Number of tubes
- P_tube · object · requis
  Tube pitch
- Q_unit · string · optionnel · Btu/hr | Gcal/hr | MBtu/hr | MW | Mcal/hr | W | cal/hr | hp
  Output heat duty unit
- R_shll · object · requis
  Shell-side fouling resistance
- R_tube · object · requis
  Tube-side fouling resistance
- T_shll · object · requis
  Shell-side temperature range [T1, T2] used for property evaluation
- T_tube · object · requis
  Tube-side temperature range [T1, T2] used for property evaluation
- V_shll · object · requis
  Shell-side volumetric flow rate
- V_tube · object · requis
  Tube-side volumetric flow rate
- k_shll · object · requis
  Shell-side fluid thermal conductivity list
- k_tube · object · requis
  Tube-side fluid thermal conductivity list
- Cp_shll · object · requis
  Shell-side fluid heat capacity list
- Cp_tube · object · requis
  Tube-side fluid heat capacity list
- Rf_unit · string · optionnel · C-h-m2/J | C-h-m2/kJ | C-h-m2/kcal | C-m2/W | C-m2/kW | F-hr-ft2/Btu | hr-ft2-F/Btu
  Output fouling resistance unit
- T1_shll · object · requis
  Shell-side inlet temperature
- T1_tube · object · requis
  Tube-side inlet temperature
- T2_shll · object · requis
  Shell-side outlet temperature
- T2_tube · object · requis
  Tube-side outlet temperature
- Unknown · string · requis · tube-V | tube-T2 | shll-V | shll-T2
  Which unknown is being solved for.
- mu_shll · object · requis
  Shell-side fluid viscosity list
- mu_tube · object · requis
  Tube-side fluid viscosity list
- S_baffle · object · requis
  Baffle spacing
- rho_shll · object · requis
  Shell-side fluid density list
- rho_tube · object · requis
  Tube-side fluid density list
- N_shllpara · object · requis
  Number of shells in parallel
- N_shllpass · object · requis
  Number of shell-side passes
- N_shllseri · object · requis
  Number of shells in series
- N_tubepass · object · requis
  Number of tube-side passes
- U_act_unit · string · optionnel · Btu/hr-ft2-F | W/m2-C | kJ/h-m2-C | kJ/s-m2-C | kcal/h-m2-C
  Output actual (fouled) overall heat transfer coefficient unit
- U_cln_unit · string · optionnel · Btu/hr-ft2-F | W/m2-C | kJ/h-m2-C | kJ/s-m2-C | kcal/h-m2-C
  Output clean overall heat transfer coefficient unit
- h_shll_unit · string · optionnel · Btu/hr-ft2 | W/m2 | kJ/h-m2 | kJ/s-m2 | kcal/h-m2
  Output shell-side film heat transfer coefficient unit
- h_tube_unit · string · optionnel · Btu/hr-ft2 | W/m2 | kJ/h-m2 | kJ/s-m2 | kcal/h-m2
  Output tube-side film heat transfer coefficient unit
- u_shll_unit · string · optionnel · MPH | cm/sec | ft/hr | ft/min | ft/sec | km/hr | m/hr | m/min
  Output shell-side velocity unit
- u_tube_unit · string · optionnel · MPH | cm/sec | ft/hr | ft/min | ft/sec | km/hr | m/hr | m/min
  Output tube-side velocity unit
Exemple d'appel
```
{"name": "HEXRF", "arguments": {"F": {}, "A_hex": {}, "k_hex": {}, "D_shll": {}, "D_tube": {}, "D_wall": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
HPADEPRESS≈ 490 tokens
Calculate depressurization gas volume and hold time for high pressure air storage vessel
Paramètres, retour & exemple (6)
Paramètres
- P1 · object · requis
  Initial pressure
- P2 · object · requis
  Final pressure
- Q2 · object · requis
  Gas consumption rate
- V1 · object · requis
  Vessel volume
- H_unit · string · optionnel · days | hours | minutes | seconds | years
  Required hold time unit
- V2_unit · string · optionnel · MSCF | Nm3 | SCF | Sm3 | kNm3 | kSCF | kSm3
  Available gas volume unit
Exemple d'appel
```
{"name": "HPADEPRESS", "arguments": {"P1": {}, "P2": {}, "Q2": {}, "V1": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
HTRINOUTEFF≈ 834 tokens
Calculate fired heater heat duty and efficiency from inlet/outlet conditions and composition
Paramètres, retour & exemple (15)
Paramètres
- HC · object · requis
  Fuel gas hydrocarbon component list (e.g. ['CH4','C2H6'])
- Tair · object · requis
  Combustion air temperature
- Trad · object · requis
  Radiant section outlet temperature
- Tstk · object · requis
  Stack gas temperature
- exO2 · object · requis
  Excess oxygen in flue gas
- mole · object · requis
  Fuel gas mole fraction list matching HC order (e.g. [0.9, 0.1])
- Mfuel · object · requis
  Fuel mass flow rate
- Tfuel · object · requis
  Fuel temperature
- Mair_unit · string · optionnel · kg/day | kg/hr | kg/min | kg/sec | klb/hr | lb/day | lb/hr | ton/day
  Output air mass flow rate unit
- Qrad_unit · string · optionnel · Btu/hr | Gcal/hr | MBtu/hr | MW | Mcal/hr | W | cal/hr | hp
  Output radiant section duty unit
- Qconv_unit · string · optionnel · Btu/hr | Gcal/hr | MBtu/hr | MW | Mcal/hr | W | cal/hr | hp
  Output convection section duty unit
- Qduty_unit · string · optionnel · Btu/hr | Gcal/hr | MBtu/hr | MW | Mcal/hr | W | cal/hr | hp
  Output total heat duty unit
- Qloss_unit · string · optionnel · Btu/hr | Gcal/hr | MBtu/hr | MW | Mcal/hr | W | cal/hr | hp
  Output heat loss unit
- MWfuel_unit · string · optionnel · g/gmol | g/mol | kg/kgmol | kg/kmol | lb/lbmol | lb/mol
  Output fuel molecular weight unit
- LHVfuel_unit · string · optionnel · Btu/lb | Btu/lbm | J/g | J/kg | cal/g | cal/kg | kJ/g | kJ/kg
  Output fuel LHV unit
Exemple d'appel
```
{"name": "HTRINOUTEFF", "arguments": {"HC": {}, "Tair": {}, "Trad": {}, "Tstk": {}, "exO2": {}, "mole": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
HTRLOSSEFF≈ 240 tokens
Calculate fired heater loss efficiency from ambient temperature, stack gas temperature and excess oxygen
Paramètres, retour & exemple (4)
Paramètres
- Ta · object · requis
  Ambient temperature
- Tg · object · requis
  Stack gas temperature
- Type · object · requis
  Fuel type
- exO2 · object · requis
  Excess oxygen
Exemple d'appel
```
{"name": "HTRLOSSEFF", "arguments": {"Ta": {}, "Tg": {}, "Type": {}, "exO2": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
LMTD≈ 270 tokens
Calculate LMTD of heat exchanger
Paramètres, retour & exemple (5)
Paramètres
- Tci · object · requis
  Cold inlet temperature
- Tco · object · requis
  Cold outlet temperature
- Thi · object · requis
  Hot inlet temperature
- Tho · object · requis
  Hot outlet temperature
- LMTD_unit · string · optionnel · C | F | K | R
  Output LMTD unit
Exemple d'appel
```
{"name": "LMTD", "arguments": {"Tci": {}, "Tco": {}, "Thi": {}, "Tho": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
LN2DEPRESS≈ 527 tokens
Calculate depressurization gas volumn abd hold time and saturation temperature for liquid nitrogen storage vessel
Paramètres, retour & exemple (7)
Paramètres
- P1 · object · requis
  Initial pressure
- P2 · object · requis
  Final pressure
- Q2 · object · requis
  Nitrogen consumption rate
- V1 · object · requis
  Tank volume
- H_unit · string · optionnel · days | hours | minutes | seconds | years
  Required hold time unit
- T1_unit · string · optionnel · C | F | K | R
  Required temperature unit
- V2_unit · string · optionnel · MSCF | Nm3 | SCF | Sm3 | kNm3 | kSCF | kSm3
  Available gas volume unit
Exemple d'appel
```
{"name": "LN2DEPRESS", "arguments": {"P1": {}, "P2": {}, "Q2": {}, "V1": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
MIXTURE≈ 1099 tokens
Primary thermodynamic property calculator. Use this tool first for all mixture property calculations. Supports hydrocarbons and non-hydrocarbon chemicals (PR EOS flash calculation).
Paramètres, retour & exemple (15)
Paramètres
- P · object · requis
  Pressure
- T · object · requis
  Temperature
- HC · array · requis
  Component list. Supported formulas or names: H2(hydrogen), CH4(methane), C2H2(acetylene), C2H4(ethylene), C2H6(ethane),C3H4(propadiene), C3H6(propene), C3H8(propane), C4H8(isobutylene), C4H10(n-butane), C5H12(pentane), C6H14(hexane), C7H16(heptane), C8H18(octane), C9H20(nonane), C10H22(decane),C11H24(undecane), C12H26(dodecane), C5H12O(MTBE), C6H6(benzene), C7H8(toluene), C8H10(o-xylene), Air, Ar(argon), N2(nitrogen), O2(oxygen), CO(carbon monoxide), CO2(carbon dioxide),H2O(water), HCl(hydrogen chloride), H2S(hydrogen sulfide), NH3(ammonia), NO2(nitrogen dioxide), N2O(nitrous oxide), N2O4(dinitrogen tetroxide), SO2(sulfur dioxide), SO3(sulfur trioxide), NaOH(sodium hydroxide). Names are case-insensitive.Examples: ['CH4','C2H6','C3H8'], ['Methane','Ethane','Propane'], ['methane','ethane','propane']
- mole · array · requis
  Mole fractions or mole amounts corresponding to HC. Automatically normalized.
- H_unit · string · optionnel · Btu/lb | Btu/lbm | J/g | J/kg | cal/g | cal/kg | kJ/g | kJ/kg
  Enthalpy unit
- S_unit · string · optionnel · Btu/lb-F | Btu/lb-R | Btu/lbm-F | Btu/lbm-R | J/g-C | J/g-K | J/kg-C | J/kg-K
  Entropy unit
- U_unit · string · optionnel · Btu/lb | Btu/lbm | J/g | J/kg | cal/g | cal/kg | kJ/g | kJ/kg
  Internal energy U unit
- k_unit · string · optionnel · Btu/hr-ft-F | Btu/hr-ft-R | Kcal/m-hr-C | Kcal/m-hr-K | W/m-C | W/m-K
  Thermal conductivity k unit
- Cp_unit · string · optionnel · Btu/lb-F | Btu/lb-R | Btu/lbm-F | Btu/lbm-R | J/g-C | J/g-K | J/kg-C | J/kg-K
  Heat capacity Cp unit
- Cv_unit · string · optionnel · Btu/lb-F | Btu/lb-R | Btu/lbm-F | Btu/lbm-R | J/g-C | J/g-K | J/kg-C | J/kg-K
  Heat capacity Cv unit
- MW_unit · string · optionnel · g/gmol | g/mol | kg/kgmol | kg/kmol | lb/lbmol | lb/mol
  Molecular weight unit
- mu_unit · string · optionnel · P | Pa-s | cP | lb/ft-sec | lb/h-ft | lbf-s/ft2 | lbm/h-ft | lbm/s-ft
  Viscosity mu unit
- rho_unit · string · optionnel · API | SG_H2O4 | SG_H2O60api | SG_H2O60nbs | g/cm3 | g/cm^3 | kg/m3 | kg/m^3
  Density unit
- Tbub_unit · string · optionnel · C | F | K | R
  Bubble point Tbub unit
- Tdew_unit · string · optionnel · C | F | K | R
  Dew point Tdew unit
Exemple d'appel
```
{"name": "MIXTURE", "arguments": {"P": {}, "T": {}, "HC": [], "mole": []}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
MtoV≈ 210 tokens
Convert mass flow rate to volumetric flow rate at standard condition
Paramètres, retour & exemple (3)
Paramètres
- M · object · requis
  Mass flow rate
- MW · object · requis
  Molecular weight
- V_unit · string · optionnel · MSCFH | Nm3/hr | SCFH | Sm3/hr | kNm3/hr | kSCFH | kSm3/hr
  Output gas volume flow unit
Exemple d'appel
```
{"name": "MtoV", "arguments": {"M": {}, "MW": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
ORIFICEGAS≈ 709 tokens
Gas orifice sizing / differential pressure / flow rate calculation based on ISO 5167 orifice. Exactly ONE of [M, dP, D2] must be set to '?' — that variable will be calculated.
Paramètres, retour & exemple (8)
Paramètres
- M · object · requis
  Gas mass flow rate. Set value='?' to calculate.
- k · object · optionnel
  Heat capacity ratio (Cp/Cv), default 1.4
- D1 · object · requis
  Pipe inside diameter
- D2 · object · requis
  Orifice bore diameter. Set value='?' to calculate.
- P1 · object · requis
  Upstream (operating) pressure
- dP · object · requis
  Differential pressure across orifice. Set value='?' to calculate.
- mu · object · requis
  Dynamic viscosity
- rho · object · requis
  Fluid density
Exemple d'appel
```
{"name": "ORIFICEGAS", "arguments": {"M": {}, "D1": {}, "D2": {}, "P1": {}, "dP": {}, "mu": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
ORIFICELIQ≈ 671 tokens
Liquid orifice sizing / differential pressure / flow rate calculation based on ISO 5167 orifice. Exactly ONE of [M, dP, D2] must be set to '?' — that variable will be calculated.
Paramètres, retour & exemple (7)
Paramètres
- M · object · requis
  Liquid mass flow rate. Set value='?' to calculate.
- D1 · object · requis
  Pipe inside diameter
- D2 · object · requis
  Orifice bore diameter. Set value='?' to calculate.
- P1 · object · requis
  Upstream (operating) pressure
- dP · object · requis
  Differential pressure across orifice. Set value='?' to calculate.
- mu · object · requis
  Dynamic viscosity
- rho · object · requis
  Fluid density
Exemple d'appel
```
{"name": "ORIFICELIQ", "arguments": {"M": {}, "D1": {}, "D2": {}, "P1": {}, "dP": {}, "mu": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
PINCHMANUAL≈ 274 tokens
Pinch analysis (minimum utilities, pinch temperatures, composite curves, grand composite curve) and heat exchanger network design by manual tick-off heuristic
Paramètres, retour & exemple (2)
Paramètres
- INPUT · object · requis
  Process streams and design parameters. Hot*/Cld* streams: {'value': [Tin, Tout, MCp], 'unit': 'kW/C'}, e.g. {'Hot1': {'value': [220, 60, 22], 'unit': 'kW/C'}, 'Cld1': {'value': [50, 210, 20], 'unit': 'kW/C'}}. All stream MCp units must match. Required: 'Tmin': {'value': 20, 'unit': 'C'} (minimum approach temperature) and 'U': {'value': 0.5, 'unit': 'kW/m2-C'} (overall heat transfer coefficient). Stream temperatures use the Tmin unit.
- OUTPUT · array · optionnel
  Optional list of output names. Default: all of T_pinch, T_hot_pinch, T_cld_pinch, Q_hot_min_utility, Q_cld_min_utility, T_hot_composite, Q_hot_composite, T_cld_composite, Q_cld_composite, T_gcc, Q_gcc. The NETWORK result is always returned.
Exemple d'appel
```
{"name": "PINCHMANUAL", "arguments": {"INPUT": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
PINCHSOLVER≈ 272 tokens
Pinch analysis (minimum utilities, pinch temperatures, composite curves, grand composite curve) and heat exchanger network design by optimization solver
Paramètres, retour & exemple (2)
Paramètres
- INPUT · object · requis
  Process streams and design parameters. Hot*/Cld* streams: {'value': [Tin, Tout, MCp], 'unit': 'kW/C'}, e.g. {'Hot1': {'value': [220, 60, 22], 'unit': 'kW/C'}, 'Cld1': {'value': [50, 210, 20], 'unit': 'kW/C'}}. All stream MCp units must match. Required: 'Tmin': {'value': 20, 'unit': 'C'} (minimum approach temperature) and 'U': {'value': 0.5, 'unit': 'kW/m2-C'} (overall heat transfer coefficient). Stream temperatures use the Tmin unit.
- OUTPUT · array · optionnel
  Optional list of output names. Default: all of T_pinch, T_hot_pinch, T_cld_pinch, Q_hot_min_utility, Q_cld_min_utility, T_hot_composite, Q_hot_composite, T_cld_composite, Q_cld_composite, T_gcc, Q_gcc. The NETWORK result is always returned.
Exemple d'appel
```
{"name": "PINCHSOLVER", "arguments": {"INPUT": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
PIPEAIR≈ 589 tokens
Calculate compressed air pipe sizing: pipe diameter, velocity, pressure drop
Paramètres, retour & exemple (8)
Paramètres
- L · object · requis
  Pipe length
- M · object · requis
  Compressed air mass flow rate
- P · object · requis
  Compressed air pressure
- T · object · requis
  Compressed air temperature
- D_unit · string · optionnel · cm | ft | in | m | micron | miles | mm
  Output pipe diameter unit
- u_unit · string · optionnel · MPH | cm/sec | ft/hr | ft/min | ft/sec | km/hr | m/hr | m/min
  Output velocity unit
- dP_unit · string · optionnel · MPa | MPag | N/m2 | N/m2g | atm | atmg | bar | barg
  Output pressure drop unit
- rho_unit · string · optionnel · API | SG_H2O4 | SG_H2O60api | SG_H2O60nbs | g/cm3 | g/cm^3 | kg/m3 | kg/m^3
  Output density unit
Exemple d'appel
```
{"name": "PIPEAIR", "arguments": {"L": {}, "M": {}, "P": {}, "T": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
PIPEFF≈ 200 tokens
Calculate Darcy friction factor based on Reynolds number and pipe roughness
Paramètres, retour & exemple (3)
Paramètres
- D · object · requis
  Pipe inside diameter
- Re · object · requis
  Reynolds number
- Piping · object · requis
  Pipe material
Exemple d'appel
```
{"name": "PIPEFF", "arguments": {"D": {}, "Re": {}, "Piping": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
PIPEFLOWGAS≈ 678 tokens
Calculate isothermal gas pipe flow: density, volumetric flow rate, mass flow rate from pressure drop
Paramètres, retour & exemple (9)
Paramètres
- D · object · requis
  Pipe inside diameter
- L · object · requis
  Pipe length
- T · object · requis
  Gas temperature
- MW · object · requis
  Gas molecular weight
- P1 · object · requis
  Upstream (inlet) pressure
- P2 · object · requis
  Downstream (outlet) pressure
- M_unit · string · optionnel · kg/day | kg/hr | kg/min | kg/sec | klb/hr | lb/day | lb/hr | ton/day
  Output mass flow unit
- Q_unit · string · optionnel · MSCFH | Nm3/hr | SCFH | Sm3/hr | kNm3/hr | kSCFH | kSm3/hr
  Output volumetric flow unit (normal conditions)
- rho_unit · string · optionnel · API | SG_H2O4 | SG_H2O60api | SG_H2O60nbs | g/cm3 | g/cm^3 | kg/m3 | kg/m^3
  Output density unit
Exemple d'appel
```
{"name": "PIPEFLOWGAS", "arguments": {"D": {}, "L": {}, "T": {}, "MW": {}, "P1": {}, "P2": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
PIPEFLOWLIQ≈ 600 tokens
Calculate liquid pipe flow: volumetric flow rate and mass flow rate from pressure drop
Paramètres, retour & exemple (7)
Paramètres
- D · object · requis
  Pipe inside diameter
- L · object · requis
  Pipe length
- P1 · object · requis
  Upstream (inlet) pressure
- P2 · object · requis
  Downstream (outlet) pressure
- rho · object · requis
  Liquid density
- M_unit · string · optionnel · kg/day | kg/hr | kg/min | kg/sec | klb/hr | lb/day | lb/hr | ton/day
  Output mass flow unit
- Q_unit · string · optionnel · L/day | L/hr | L/min | L/sec | USGPH | USGPM | barrel/day | barrel/hr
  Output volumetric flow unit
Exemple d'appel
```
{"name": "PIPEFLOWLIQ", "arguments": {"D": {}, "L": {}, "P1": {}, "P2": {}, "rho": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
PIPEINSUL≈ 705 tokens
Calculate optimal pipe insulation thickness to limit outer surface temperature (burn protection) and minimise heat loss. Uses cylindrical heat conduction + external convection model, solved via scipy.optimize.brentq. Returns exact minimum thickness and nearest commercial 5 mm step.
Paramètres, retour & exemple (12)
Paramètres
- Ta · object · requis
  Ambient (outdoor) temperature
- Tf · object · requis
  Fluid / pipe outer surface temperature
- ha · object · requis
  External (air-side) convection coefficient
- NPS · object · requis
  Nominal Pipe Size in inches (ASME B36.10).
- Tmax · object · requis
  Maximum allowable insulation outer surface temperature (burn-prevention limit = 50 °C per EN ISO 13732-1)
- kins · object · requis
  Insulation thermal conductivity
- r2_unit · string · optionnel · cm | ft | in | m | micron | miles | mm
  Desired Pipe outer radius output unit
- r3_unit · string · optionnel · cm | ft | in | m | micron | miles | mm
  Desired Insulation outer radius output unit
- tins_unit · string · optionnel · cm | ft | in | m | micron | miles | mm
  Desired Insulation thickness output unit
- Dpipe_unit · string · optionnel · cm | ft | in | m | micron | miles | mm
  Desired Pipe OD output unit
- Qloss_unit · string · optionnel · W/m | kW/m | BTU/hr-ft
  Desired Heat loss output unit
- Tsurf_unit · string · optionnel · C | F | K | R
  Desired Surface temperature output unit
Exemple d'appel
```
{"name": "PIPEINSUL", "arguments": {"Ta": {}, "Tf": {}, "ha": {}, "NPS": {}, "Tmax": {}, "kins": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
PIPENITROGEN≈ 584 tokens
Calculate nitrogen pipe sizing: pipe diameter, velocity, pressure drop
Paramètres, retour & exemple (8)
Paramètres
- L · object · requis
  Pipe length
- M · object · requis
  Nitrogen mass flow rate
- P · object · requis
  Nitrogen pressure
- T · object · requis
  Nitrogen temperature
- D_unit · string · optionnel · cm | ft | in | m | micron | miles | mm
  Output pipe diameter unit
- u_unit · string · optionnel · MPH | cm/sec | ft/hr | ft/min | ft/sec | km/hr | m/hr | m/min
  Output velocity unit
- dP_unit · string · optionnel · MPa | MPag | N/m2 | N/m2g | atm | atmg | bar | barg
  Output pressure drop unit
- rho_unit · string · optionnel · API | SG_H2O4 | SG_H2O60api | SG_H2O60nbs | g/cm3 | g/cm^3 | kg/m3 | kg/m^3
  Output density unit
Exemple d'appel
```
{"name": "PIPENITROGEN", "arguments": {"L": {}, "M": {}, "P": {}, "T": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
PIPESTEAM≈ 580 tokens
Calculate steam pipe sizing: pipe diameter, velocity, pressure drop
Paramètres, retour & exemple (8)
Paramètres
- L · object · requis
  Pipe length
- M · object · requis
  Steam mass flow rate
- P · object · requis
  Steam pressure
- T · object · requis
  Steam temperature
- D_unit · string · optionnel · cm | ft | in | m | micron | miles | mm
  Output pipe diameter unit
- u_unit · string · optionnel · MPH | cm/sec | ft/hr | ft/min | ft/sec | km/hr | m/hr | m/min
  Output velocity unit
- dP_unit · string · optionnel · MPa | MPag | N/m2 | N/m2g | atm | atmg | bar | barg
  Output pressure drop unit
- rho_unit · string · optionnel · API | SG_H2O4 | SG_H2O60api | SG_H2O60nbs | g/cm3 | g/cm^3 | kg/m3 | kg/m^3
  Output density unit
Exemple d'appel
```
{"name": "PIPESTEAM", "arguments": {"L": {}, "M": {}, "P": {}, "T": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
PIPEWATER≈ 580 tokens
Calculate water pipe sizing: pipe diameter, velocity, pressure drop
Paramètres, retour & exemple (8)
Paramètres
- L · object · requis
  Pipe length
- M · object · requis
  Water mass flow rate
- P · object · requis
  Water pressure
- T · object · requis
  Water temperature
- D_unit · string · optionnel · cm | ft | in | m | micron | miles | mm
  Output pipe diameter unit
- u_unit · string · optionnel · MPH | cm/sec | ft/hr | ft/min | ft/sec | km/hr | m/hr | m/min
  Output velocity unit
- dP_unit · string · optionnel · MPa | MPag | N/m2 | N/m2g | atm | atmg | bar | barg
  Output pressure drop unit
- rho_unit · string · optionnel · API | SG_H2O4 | SG_H2O60api | SG_H2O60nbs | g/cm3 | g/cm^3 | kg/m3 | kg/m^3
  Output density unit
Exemple d'appel
```
{"name": "PIPEWATER", "arguments": {"L": {}, "M": {}, "P": {}, "T": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
PSVGAS≈ 693 tokens
Calculate required PSV (pressure safety valve) relief area for gas/vapor service per API 520
Paramètres, retour & exemple (10)
Paramètres
- M · object · requis
  Relieving mass flow rate
- k · object · optionnel
  Heat capacity ratio (Cp/Cv), default 1.4
- Kb · object · optionnel
  Capacity correction factor for back pressure, default 1.0
- Kc · object · optionnel
  Combination correction factor (rupture disk), default 1.0
- Kd · object · optionnel
  Effective coefficient of discharge, default 0.975
- MW · object · requis
  Gas/vapor molecular weight
- P1 · object · requis
  Upstream relieving pressure (set pressure + overpressure + atm)
- P2 · object · requis
  Downstream (back) pressure
- T1 · object · requis
  Relieving temperature
- A_unit · string · optionnel · cm2 | ft2 | in2 | m2
  Output relief area unit
Exemple d'appel
```
{"name": "PSVGAS", "arguments": {"M": {}, "MW": {}, "P1": {}, "P2": {}, "T1": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
PSVLIQ≈ 696 tokens
Calculate required PSV (pressure safety valve) relief area for liquid service per API 520
Paramètres, retour & exemple (10)
Paramètres
- M · object · requis
  Relieving mass flow rate
- Kc · object · optionnel
  Combination correction factor (rupture disk), default 1.0
- Kd · object · optionnel
  Effective coefficient of discharge, default 0.65
- Kv · object · optionnel
  Viscosity correction factor, default 1.0
- Kw · object · optionnel
  Back pressure correction factor (balanced bellows), default 1.0
- P1 · object · requis
  Upstream relieving pressure (set pressure + overpressure + atm)
- P2 · object · requis
  Downstream (back) pressure
- rho · object · requis
  Liquid density
- Pover · object · optionnel
  Overpressure fraction (e.g. 0.1 = 10%), default 0.1
- A_unit · string · optionnel · cm2 | ft2 | in2 | m2
  Output relief area unit
Exemple d'appel
```
{"name": "PSVLIQ", "arguments": {"M": {}, "P1": {}, "P2": {}, "rho": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
PSVSTEAM≈ 463 tokens
Calculate required PSV (pressure safety valve) relief area for steam service per API 520
Paramètres, retour & exemple (7)
Paramètres
- M · object · requis
  Relieving mass flow rate
- Kb · object · optionnel
  Capacity correction factor for back pressure, default 1.0
- Kc · object · optionnel
  Combination correction factor (rupture disk), default 1.0
- Kd · object · optionnel
  Effective coefficient of discharge, default 0.975
- P1 · object · requis
  Upstream relieving pressure (set pressure + overpressure + atm)
- T1 · object · requis
  Relieving temperature
- A_unit · string · optionnel · cm2 | ft2 | in2 | m2
  Output relief area unit
Exemple d'appel
```
{"name": "PSVSTEAM", "arguments": {"M": {}, "P1": {}, "T1": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
PSYCHROMETRIC≈ 501 tokens
Psychrometric properties of moist air
Paramètres, retour & exemple (10)
Paramètres
- BP · object · requis
- DB · object · requis
- DP · object · optionnel
- RH · object · optionnel
- WB · object · optionnel
- H_unit · string · optionnel · Btu/lb | Btu/lbm | J/g | J/kg | cal/g | cal/kg | kJ/g | kJ/kg
  Enthalpy output unit (HDA/HWA)
- V_unit · string · optionnel · cm3/g | cm^3/g | ft3/lb | ft^3/lb | m3/kg | m^3/kg
  Specific volume unit (VDA/VWA)
- DP_unit · string · optionnel · C | F | K | R
  Dew point temperature output unit
- WB_unit · string · optionnel · C | F | K | R
  Wet bulb temperature output unit
- rho_unit · string · optionnel · API | SG_H2O4 | SG_H2O60api | SG_H2O60nbs | g/cm3 | g/cm^3 | kg/m3 | kg/m^3
  Density output unit (DDA/DWA)
Exemple d'appel
```
{"name": "PSYCHROMETRIC", "arguments": {"BP": {}, "DB": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
PTV≈ 242 tokens
Calculate gas molar volume using equation of state
Paramètres, retour & exemple (3)
Paramètres
- P · object · requis
  Pressure
- T · object · requis
  Temperature
- V_unit · string · optionnel · L | cm3 | ft3 | in3 | m3 | mL
  Output molar volume unit
Exemple d'appel
```
{"name": "PTV", "arguments": {"P": {}, "T": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
PUMPBHP≈ 535 tokens
Calculate pump brake horsepower
Paramètres, retour & exemple (6)
Paramètres
- Q · object · requis
  Volumetric flow rate
- P1 · object · requis
  Inlet pressure
- P2 · object · requis
  Outlet pressure
- Eff · object · requis
  Pump efficiency
- rho · object · requis
  Fluid density
- BHP_unit · string · optionnel · Btu/hr | Gcal/hr | MBtu/hr | MW | Mcal/hr | W | cal/hr | hp
  Output power unit
Exemple d'appel
```
{"name": "PUMPBHP", "arguments": {"Q": {}, "P1": {}, "P2": {}, "Eff": {}, "rho": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
Pmean≈ 434 tokens
Calculate mean pressure between inlet and outlet
Paramètres, retour & exemple (4)
Paramètres
- P1 · object · requis
  Inlet pressure
- P2 · object · requis
  Outlet pressure
- Fluid · object · requis
  Fluid type (gas or liquid)
- Pmean_unit · string · optionnel · MPa | MPag | N/m2 | N/m2g | atm | atmg | bar | barg
  Output mean pressure unit
Exemple d'appel
```
{"name": "Pmean", "arguments": {"P1": {}, "P2": {}, "Fluid": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
REFRIGERANT≈ 742 tokens
Calculate refrigerant thermodynamic properties using CoolProp. Provide Fluid name and any 2 state variables from: T, P, rho, H, S, U. Returns all remaining properties: T, P, rho, H, S, U, Cp, Cv, viscosity, conductivity, molecular weight.
Paramètres, retour & exemple (18)
Paramètres
- H · object · optionnel
  Specific Enthalpy (INPUT if known). Units: J/kg, kJ/kg
- P · object · optionnel
  Pressure (INPUT if known). Units: Pa, kPa, MPa, bar, psi
- S · object · optionnel
  Specific Entropy (INPUT if known). Units: J/kg-K, kJ/kg-K
- T · object · optionnel
  Temperature (INPUT if known). Units: K, C, F
- U · object · optionnel
  Specific Internal Energy (INPUT if known). Units: J/kg, kJ/kg
- rho · object · optionnel
  Density (INPUT if known). Units: kg/m3
- Fluid · object · requis
  Refrigerant name. Supported: R134a, R22, R32, R410A, R407C, R1234yf, R1234ze(E), Ammonia(=NH3), CarbonDioxide(=CO2)
- C_unit · string · optionnel
  Desired Cp output unit
- H_unit · string · optionnel
  Desired Enthalpy output unit
- L_unit · string · optionnel
  Desired Conductivity output unit
- M_unit · string · optionnel
  Desired Molecular Weight output unit
- O_unit · string · optionnel
  Desired Cv output unit
- P_unit · string · optionnel
  Desired Pressure output unit
- S_unit · string · optionnel
  Desired Entropy output unit
- T_unit · string · optionnel
  Desired Temperature output unit
- U_unit · string · optionnel
  Desired Internal Energy unit
- V_unit · string · optionnel
  Desired Viscosity output unit
- rho_unit · string · optionnel
  Desired Density output unit
Exemple d'appel
```
{"name": "REFRIGERANT", "arguments": {"Fluid": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
SOLVE≈ 70 tokens
Solve nonlinear equations with unknown variables using fsolve
Paramètres, retour & exemple (3)
Paramètres
- INPUT · object · requis
- OUTPUT · object · requis
- FORMULA · object · requis
Exemple d'appel
```
{"name": "SOLVE", "arguments": {"INPUT": {}, "OUTPUT": {}, "FORMULA": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
STEAM≈ 838 tokens
Calculate thermodynamic and transport properties of steam based on IAPWS
Paramètres, retour & exemple (12)
Paramètres
- P · object · requis
  Pressure
- T · object · requis
  Temperature
- H_unit · string · optionnel · Btu/lb | Btu/lbm | J/g | J/kg | cal/g | cal/kg | kJ/g | kJ/kg
  Enthalpy unit
- S_unit · string · optionnel · Btu/lb-F | Btu/lb-R | Btu/lbm-F | Btu/lbm-R | J/g-C | J/g-K | J/kg-C | J/kg-K
  Entropy unit
- U_unit · string · optionnel · Btu/lb | Btu/lbm | J/g | J/kg | cal/g | cal/kg | kJ/g | kJ/kg
  Internal energy unit
- k_unit · string · optionnel · Btu/hr-ft-F | Btu/hr-ft-R | Kcal/m-hr-C | Kcal/m-hr-K | W/m-C | W/m-K
  Thermal conductivity unit
- Cp_unit · string · optionnel · Btu/lb-F | Btu/lb-R | Btu/lbm-F | Btu/lbm-R | J/g-C | J/g-K | J/kg-C | J/kg-K
  Cp unit
- Cv_unit · string · optionnel · Btu/lb-F | Btu/lb-R | Btu/lbm-F | Btu/lbm-R | J/g-C | J/g-K | J/kg-C | J/kg-K
  Cv unit
- mu_unit · string · optionnel · P | Pa-s | cP | lb/ft-sec | lb/h-ft | lbf-s/ft2 | lbm/h-ft | lbm/s-ft
  Viscosity unit
- rho_unit · string · optionnel · API | SG_H2O4 | SG_H2O60api | SG_H2O60nbs | g/cm3 | g/cm^3 | kg/m3 | kg/m^3
  Density unit
- Psat_unit · string · optionnel · MPa | MPag | N/m2 | N/m2g | atm | atmg | bar | barg
  Saturation pressure unit
- Tsat_unit · string · optionnel · C | F | K | R
  Saturation temperature unit
Exemple d'appel
```
{"name": "STEAM", "arguments": {"P": {}, "T": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
STEAMFLASH≈ 402 tokens
Calculate flash steam flow from pressure reduction
Paramètres, retour & exemple (4)
Paramètres
- Mc · object · requis
  Condensate flow rate
- Pc · object · requis
  Condensate pressure
- Ps · object · requis
  Steam header pressure
- Ms_unit · string · optionnel · kg/day | kg/hr | kg/min | kg/sec | klb/hr | lb/day | lb/hr | ton/day
  Output flash steam flow unit
Exemple d'appel
```
{"name": "STEAMFLASH", "arguments": {"Mc": {}, "Pc": {}, "Ps": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
STEAMLEAK≈ 561 tokens
Calculate steam leak mass flow and flow condition (CHOKED / SUBCRITICAL) based on upstream and downstream conditions
Paramètres, retour & exemple (7)
Paramètres
- h · object · requis
  Pin-hole Diameter
- Cd · object · optionnel
  Discharge coefficient (default: 0.80)
- P1 · object · requis
  Upstream Pressure
- P2 · object · requis
  Downstream Pressure
- T1 · object · requis
  Upstream Temperature
- T2 · object · requis
  Downstream Temperature
- M_unit · string · optionnel · kg/day | kg/hr | kg/min | kg/sec | klb/hr | lb/day | lb/hr | ton/day
  Output mass flow unit
Exemple d'appel
```
{"name": "STEAMLEAK", "arguments": {"h": {}, "P1": {}, "P2": {}, "T1": {}, "T2": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
STEAMPH≈ 361 tokens
Calculate mass flow from pin-hole on the steam piping
Paramètres, retour & exemple (5)
Paramètres
- P · object · requis
  Pressure
- T · object · requis
  Temperature
- h · object · requis
  pin-hole D
- Cd · object · optionnel
  Discharge coefficient (default: 0.80)
- M_unit · string · optionnel · kg/day | kg/hr | kg/min | kg/sec | klb/hr | lb/day | lb/hr | ton/day
  Output mass flow unit
Exemple d'appel
```
{"name": "STEAMPH", "arguments": {"P": {}, "T": {}, "h": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
STGEFF≈ 1206 tokens
Calculate multistage steam turbine isentropic efficiency
Paramètres, retour & exemple (17)
Paramètres
- E · object · requis
  Actual generator output
- M1 · object · requis
  Main steam flow
- M2 · object · optionnel
  Extraction steam flow #1
- M3 · object · optionnel
  Extraction steam flow #2
- M4 · object · optionnel
  Extraction steam flow #3
- M5 · object · optionnel
  Extraction steam flow #4
- P1 · object · requis
  Stage pressure #1
- P2 · object · requis
  Stage pressure #2
- P3 · object · optionnel
  Stage pressure #3
- P4 · object · optionnel
  Stage pressure #4
- P5 · object · optionnel
  Stage pressure #5
- T1 · object · requis
  Stage temperature #1
- T2 · object · requis
  Stage temperature #2
- T3 · object · optionnel
  Stage temperature #3
- T4 · object · optionnel
  Stage temperature #4
- T5 · object · optionnel
  Stage temperature #5
- Eff_unit · string · optionnel · %
Exemple d'appel
```
{"name": "STGEFF", "arguments": {"E": {}, "M1": {}, "P1": {}, "P2": {}, "T1": {}, "T2": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
STMDEPRESS≈ 496 tokens
Calculate depressurization steam volumn and hold time for steam accumulator
Paramètres, retour & exemple (6)
Paramètres
- M2 · object · requis
  Steam consumption rate
- P1 · object · requis
  Initial pressure
- P2 · object · requis
  Final pressure
- V1 · object · requis
  Accumulator volume
- H_unit · string · optionnel · days | hours | minutes | seconds | years
  Required hold time unit
- V2_unit · string · optionnel · g | kg | klb | lb | oz | ton | ton(long) | ton(short)
  Available steam amount unit
Exemple d'appel
```
{"name": "STMDEPRESS", "arguments": {"M2": {}, "P1": {}, "P2": {}, "V1": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
TBNEFF≈ 413 tokens
Calculate steam turbine isentropic efficiency
Paramètres, retour & exemple (5)
Paramètres
- Pi · object · requis
  Inlet pressure
- Po · object · requis
  Outlet pressure
- Ti · object · requis
  Inlet temperature
- To · object · requis
  Actual outlet temperature
- Eff_unit · string · optionnel · %
  Output efficiency unit
Exemple d'appel
```
{"name": "TBNEFF", "arguments": {"Pi": {}, "Po": {}, "Ti": {}, "To": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
VENTURIGAS≈ 722 tokens
Gas Venturi tube sizing / differential pressure / flow rate calculation based on ISO 5167 Venturi meter (as cast convergent venturi tube). Exactly ONE of [M, dP, D2] must be set to '?' — that variable will be calculated.
Paramètres, retour & exemple (8)
Paramètres
- M · object · requis
  Gas mass flow rate. Set value='?' to calculate.
- k · object · optionnel
  Heat capacity ratio (Cp/Cv), default 1.4
- D1 · object · requis
  Pipe inside diameter
- D2 · object · requis
  Venturi throat diameter. Set value='?' to calculate.
- P1 · object · requis
  Upstream (operating) pressure
- dP · object · requis
  Differential pressure across Venturi meter. Set value='?' to calculate.
- mu · object · requis
  Dynamic viscosity
- rho · object · requis
  Fluid density
Exemple d'appel
```
{"name": "VENTURIGAS", "arguments": {"M": {}, "D1": {}, "D2": {}, "P1": {}, "dP": {}, "mu": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
VENTURILIQ≈ 684 tokens
Liquid Venturi tube sizing / differential pressure / flow rate calculation based on ISO 5167 Venturi meter (as cast convergent venturi tube). Exactly ONE of [M, dP, D2] must be set to '?' — that variable will be calculated.
Paramètres, retour & exemple (7)
Paramètres
- M · object · requis
  Liquid mass flow rate. Set value='?' to calculate.
- D1 · object · requis
  Pipe inside diameter
- D2 · object · requis
  Venturi throat diameter. Set value='?' to calculate.
- P1 · object · requis
  Upstream (operating) pressure
- dP · object · requis
  Differential pressure across Venturi meter. Set value='?' to calculate.
- mu · object · requis
  Dynamic viscosity
- rho · object · requis
  Fluid density
Exemple d'appel
```
{"name": "VENTURILIQ", "arguments": {"M": {}, "D1": {}, "D2": {}, "P1": {}, "dP": {}, "mu": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
VtoM≈ 221 tokens
Convert volumetric flow rate to mass flow rate at standard condition and normal condition Sm3/hr, Nm3/hr, SCFH
Paramètres, retour & exemple (3)
Paramètres
- V · object · requis
  Volumetric flow rate
- MW · object · requis
  Molecular weight
- M_unit · string · optionnel · kg/day | kg/hr | kg/min | kg/sec | klb/hr | lb/day | lb/hr | ton/day
  Output mass flow unit
Exemple d'appel
```
{"name": "VtoM", "arguments": {"V": {}, "MW": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
advDVR≈ 255 tokens
Advanced Data Validation and Reconciliation including gross error detection and elimation
Paramètres, retour & exemple (3)
Paramètres
- ACCURACY · object · requis
  Measurement accuracy in %. Format: {TAG: {value: number, unit: '%'}}. Example: {A: {value: 5, unit: '%'}}
- EQUATION · object · requis
  Constraint equations. Format: {EQ1: 'A=B+C', EQ2: 'C=D+E'}. Each value is an equation string with '=' separator.
- MEASURED · object · requis
  Measured values. Format: {TAG: {value: number, unit: string}}. Example: {A: {value: 100, unit: ''}}
Exemple d'appel
```
{"name": "advDVR", "arguments": {"ACCURACY": {}, "EQUATION": {}, "MEASURED": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```
advECONOMIC≈ 313 tokens
Advanced Economic analysis with inflation, depreciation, and tax: NPV, IRR, Simple Payback, Profitability Index, NCF
Paramètres, retour & exemple (1)
Paramètres
- INPUT · object · requis
Exemple d'appel
```
{"name": "advECONOMIC", "arguments": {"INPUT": {}}}
```
Exemple de retour
```
{"content": [{"type": "text", "text": "…"}]}
```

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