com.engscript/mcp

Name: com.engscript/mcp
Author: com.engscript

MCPCommunitylive

v1.0.0com.engscriptUnknownAktualisiert vor 1 Mon.

Engineering calculation MCP server for oil and gas engineering applications.

Endpunkt-Statuslive

geprüft vor 23 Std. · 960 ms

100 % der letzten 5 Prüfungen haben diesen Endpunkt erreicht

Läuft in

ClaudeCursorCopilotChatGPTGemini

Abgeleitet aus den Transporten, die dieser Eintrag deklariert (streamable-http). Ein Client, der hier nicht steht, ist damit nicht ausgeschlossen — Forge kann ihn nur nicht bestätigen.

Automatisch aus öffentlichen Quellen indexiert. Vom Entwickler auf Forge noch nicht verifiziert.Diesen Eintrag beanspruchen →

vor 1 Mon.Letzte Aktualisierung

Paket

Autorcom.engscript

LizenzUnknown

Version1.0.0

Quellemcp-registry

SBOMCycloneDX 1.6 ↓

Trust-Status

60/100Gut

✓Im Forge-Index gelistet+10/10

—Publisher-Identität verifiziert+0/30

→ Publisher: für diesen Eintrag ist kein Repository hinterlegt, daher kann `forge publish` die Inhaberschaft nicht automatisch prüfen. Nutze oben „Diesen Eintrag beanspruchen“ — Forge prüft diese Fälle von Hand.

—Domain-Verifizierung+0/10

→ Für diesen Eintragstyp derzeit nicht verfügbar — die Domain-Prüfung läuft heute nur für npm-gestützte Pakete, diese Zeile lässt sich hier also noch nicht erreichen, unabhängig davon, was auf der Domain liegt.

✓Prompt-Injection-Scan · sauber+30/30

✓Obfuskations-/Exfiltrations-Scan · sauber+20/20

StatusVon der Community indexiert

PublisherNicht verifiziert

SignaturNicht signiert

Domain—

Herkunft—

AbhängigkeitenNicht auditiert

Tool-Oberfläche58 Tools · keines privilegiert

Sicherheits-Scan✓ Saubervlive · heuteWie gut funktioniert dieser Scan?

EvaluierungenKeine

Indexiert14. Aug. 2026

Die Verifizierung bestätigt die Identität des Publishers (die Inhaberschaft am Repo), nicht die Sicherheit des Codes. Der Sicherheits-Scan deckt bekannte CVEs und verdächtige Installationsskripte ab.

Tools

58 Tools · keines privilegiert

Live am Endpunkt des Anbieters beobachtet23h ago

Aus einem echten MCP-Handshake initialize → tools/list gegen den deklarierten Endpunkt gelesen. Es wurde nie ein Tool aufgerufen — tools/list ist der lesende Introspektionsaufruf, den das Protokoll dafür vorsieht. Es spiegelt wider, was der Server in diesem Moment angeboten hat; ein gehosteter Endpunkt ist an keine Version gebunden und kann sich ohne Ankündigung ändern.

https://engscript.com/mcp58 Tools · 960 ms

Tools filternNur privilegierte

MIXTUREPrimary thermodynamic property calculator. Use this tool first for all mixture property calculations. Supports hydrocarbons and non-hydrocarbon chemicals (PR EOS flash calculation).

Primary thermodynamic property calculator. Use this tool first for all mixture property calculations. Supports hydrocarbons and non-hydrocarbon chemicals (PR EOS flash calculation).

Parameter	Typ	Beschreibung
HC*	array	Component list. Supported formulas or names: H2(hydrogen), CH4(methane), C2H2(acetylene), C2H4(ethylene), C2H6(ethane),C3H4(propadiene), C3H6(propene), C3H8(pr…
mole*	array	Mole fractions or mole amounts corresponding to HC. Automatically normalized.
P*	object	Pressure
T*	object	Temperature
Tbub_unit	string	Bubble point Tbub unit
Tdew_unit	string	Dew point Tdew unit
MW_unit	string	Molecular weight unit
H_unit	string	Enthalpy unit
S_unit	string	Entropy unit
U_unit	string	Internal energy U unit
Cp_unit	string	Heat capacity Cp unit
Cv_unit	string	Heat capacity Cv unit
rho_unit	string	Density unit
mu_unit	string	Viscosity mu unit
k_unit	string	Thermal conductivity k unit

CARBONCalculate thermodynamic properties of hydrocarbon mixture. Supports hydrocarbons and non-hydrocarbon chemicals (PR EOS flash calculation).

Calculate thermodynamic properties of hydrocarbon mixture. Supports hydrocarbons and non-hydrocarbon chemicals (PR EOS flash calculation).

Parameter	Typ	Beschreibung
HC*	array	List of component formula strings. Supported: H2, CH4, C2H2, C2H4, C2H6, C3H4, C3H6, C3H8, C4H8, C4H10, C5H12, C6H14, C7H16, C8H18, C9H20, C10H22, C6H6, C7H8,…
mole*	array	Mole fraction list corresponding to HC, e.g. [0.85, 0.10, 0.03, 0.02]
P*	object	Pressure
T*	object	Temperature
Tbub_unit	string	Bubble point temperature unit
Tdew_unit	string	Dew point temperature unit
H_unit	string	Enthalpy unit
S_unit	string	Entropy unit
Cp_unit	string	Cp unit
Cv_unit	string	Cv unit
rho_unit	string	Density unit

STEAMCalculate thermodynamic and transport properties of steam based on IAPWS

Calculate thermodynamic and transport properties of steam based on IAPWS

Parameter	Typ	Beschreibung
P*	object	Pressure
T*	object	Temperature
Psat_unit	string	Saturation pressure unit
Tsat_unit	string	Saturation temperature unit
H_unit	string	Enthalpy unit
S_unit	string	Entropy unit
rho_unit	string	Density unit
U_unit	string	Internal energy unit
mu_unit	string	Viscosity unit
k_unit	string	Thermal conductivity unit
Cp_unit	string	Cp unit
Cv_unit	string	Cv unit

PSYCHROMETRICPsychrometric properties of moist air

Psychrometric properties of moist air

Parameter	Typ	Beschreibung
BP*	object	—
DB*	object	—
WB	object	—
DP	object	—
RH	object	—
WB_unit	string	Wet bulb temperature output unit
DP_unit	string	Dew point temperature output unit
H_unit	string	Enthalpy output unit (HDA/HWA)
rho_unit	string	Density output unit (DDA/DWA)
V_unit	string	Specific volume unit (VDA/VWA)

FUELGASCalculate MW, LHV and HHV of fuel gas from composition

Calculate MW, LHV and HHV of fuel gas from composition

Parameter	Typ	Beschreibung
HC*	array	List of fuel component formula strings, e.g. ['CH4', 'C2H6', 'H2', 'N2']
mole*	array	Mole fraction list corresponding to HC, e.g. [0.90, 0.05, 0.03, 0.02]
MW_unit	string	MW output unit
LHV_unit	string	LHV output unit
HHV_unit	string	HHV output unit

FLUEGASCalculate enthalpy of flue gas from composition

Calculate enthalpy of flue gas from composition

Parameter	Typ	Beschreibung
HC*	array	List of fuel component formula strings, e.g. ['CH4', 'C2H6', 'N2']
mole*	array	Mole fraction list corresponding to HC, e.g. [0.90, 0.05, 0.05]
Tb*	object	Base temperature
Tg*	object	Flue gas temperature
MW_unit	string	MW output unit
Cp_unit	string	Cp output unit
dH_unit	string	Enthalpy output unit

EMISSIONFACTORCalculate CO2 emission conversion factor from gas composition

Calculate CO2 emission conversion factor from gas composition

Parameter	Typ	Beschreibung
HC*	array	List of fuel component formula strings, e.g. ['CH4', 'C3H8', 'N2', 'CO2']
mole*	array	Mole fraction list corresponding to HC, e.g. [0.88, 0.05, 0.04, 0.03]
ECF_unit	string	Emission factor output unit

REFRIGERANTCalculate 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.

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.

Parameter	Typ	Beschreibung
Fluid*	object	Refrigerant name. Supported: R134a, R22, R32, R410A, R407C, R1234yf, R1234ze(E), Ammonia(=NH3), CarbonDioxide(=CO2)
T	object	Temperature (INPUT if known). Units: K, C, F
P	object	Pressure (INPUT if known). Units: Pa, kPa, MPa, bar, psi
H	object	Specific Enthalpy (INPUT if known). Units: J/kg, kJ/kg
S	object	Specific Entropy (INPUT if known). Units: J/kg-K, kJ/kg-K
U	object	Specific Internal Energy (INPUT if known). Units: J/kg, kJ/kg
rho	object	Density (INPUT if known). Units: kg/m3
T_unit	string	Desired Temperature output unit
P_unit	string	Desired Pressure output unit
M_unit	string	Desired Molecular Weight output unit
H_unit	string	Desired Enthalpy output unit
S_unit	string	Desired Entropy output unit
U_unit	string	Desired Internal Energy unit
C_unit	string	Desired Cp output unit
O_unit	string	Desired Cv output unit
rho_unit	string	Desired Density output unit
V_unit	string	Desired Viscosity output unit
L_unit	string	Desired Conductivity output unit

PTVCalculate gas molar volume using equation of state

Calculate gas molar volume using equation of state

Parameter	Typ	Beschreibung
P*	object	Pressure
T*	object	Temperature
V_unit	string	Output molar volume unit

MtoVConvert mass flow rate to volumetric flow rate at standard condition

Convert mass flow rate to volumetric flow rate at standard condition

Parameter	Typ	Beschreibung
M*	object	Mass flow rate
MW*	object	Molecular weight
V_unit	string	Output gas volume flow unit

VtoMConvert volumetric flow rate to mass flow rate at standard condition and normal condition Sm3/hr, Nm3/hr, SCFH

Convert volumetric flow rate to mass flow rate at standard condition and normal condition Sm3/hr, Nm3/hr, SCFH

Parameter	Typ	Beschreibung
V*	object	Volumetric flow rate
MW*	object	Molecular weight
M_unit	string	Output mass flow unit

PmeanCalculate mean pressure between inlet and outlet

Calculate mean pressure between inlet and outlet

Parameter	Typ	Beschreibung
Fluid*	object	Fluid type (gas or liquid)
P1*	object	Inlet pressure
P2*	object	Outlet pressure
Pmean_unit	string	Output mean pressure unit

PIPEFFCalculate Darcy friction factor based on Reynolds number and pipe roughness

Calculate Darcy friction factor based on Reynolds number and pipe roughness

Parameter	Typ	Beschreibung
Piping*	object	Pipe material
D*	object	Pipe inside diameter
Re*	object	Reynolds number

STEAMPHCalculate mass flow from pin-hole on the steam piping

Calculate mass flow from pin-hole on the steam piping

Parameter	Typ	Beschreibung
P*	object	Pressure
T*	object	Temperature
h*	object	pin-hole D
Cd	object	Discharge coefficient (default: 0.80)
M_unit	string	Output mass flow unit

STEAMLEAKCalculate steam leak mass flow and flow condition (CHOKED / SUBCRITICAL) based on upstream and downstream conditions

Calculate steam leak mass flow and flow condition (CHOKED / SUBCRITICAL) based on upstream and downstream conditions

Parameter	Typ	Beschreibung
P1*	object	Upstream Pressure
P2*	object	Downstream Pressure
T1*	object	Upstream Temperature
T2*	object	Downstream Temperature
h*	object	Pin-hole Diameter
Cd	object	Discharge coefficient (default: 0.80)
M_unit	string	Output mass flow unit

PIPEINSULCalculate 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.

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.

Parameter	Typ	Beschreibung
NPS*	object	Nominal Pipe Size in inches (ASME B36.10).
Tf*	object	Fluid / pipe outer surface temperature
Ta*	object	Ambient (outdoor) temperature
Tmax*	object	Maximum allowable insulation outer surface temperature (burn-prevention limit = 50 °C per EN ISO 13732-1)
kins*	object	Insulation thermal conductivity
ha*	object	External (air-side) convection coefficient
Dpipe_unit	string	Desired Pipe OD output unit
tins_unit	string	Desired Insulation thickness output unit
r2_unit	string	Desired Pipe outer radius output unit
r3_unit	string	Desired Insulation outer radius output unit
Tsurf_unit	string	Desired Surface temperature output unit
Qloss_unit	string	Desired Heat loss output unit

PIPESTEAMCalculate steam pipe sizing: pipe diameter, velocity, pressure drop

Calculate steam pipe sizing: pipe diameter, velocity, pressure drop

Parameter	Typ	Beschreibung
P*	object	Steam pressure
T*	object	Steam temperature
M*	object	Steam mass flow rate
L*	object	Pipe length
D_unit	string	Output pipe diameter unit
u_unit	string	Output velocity unit
dP_unit	string	Output pressure drop unit
rho_unit	string	Output density unit

PIPEWATERCalculate water pipe sizing: pipe diameter, velocity, pressure drop

Calculate water pipe sizing: pipe diameter, velocity, pressure drop

Parameter	Typ	Beschreibung
P*	object	Water pressure
T*	object	Water temperature
M*	object	Water mass flow rate
L*	object	Pipe length
D_unit	string	Output pipe diameter unit
u_unit	string	Output velocity unit
dP_unit	string	Output pressure drop unit
rho_unit	string	Output density unit

PIPEAIRCalculate compressed air pipe sizing: pipe diameter, velocity, pressure drop

Calculate compressed air pipe sizing: pipe diameter, velocity, pressure drop

Parameter	Typ	Beschreibung
P*	object	Compressed air pressure
T*	object	Compressed air temperature
M*	object	Compressed air mass flow rate
L*	object	Pipe length
D_unit	string	Output pipe diameter unit
u_unit	string	Output velocity unit
dP_unit	string	Output pressure drop unit
rho_unit	string	Output density unit

PIPENITROGENCalculate nitrogen pipe sizing: pipe diameter, velocity, pressure drop

Calculate nitrogen pipe sizing: pipe diameter, velocity, pressure drop

Parameter	Typ	Beschreibung
P*	object	Nitrogen pressure
T*	object	Nitrogen temperature
M*	object	Nitrogen mass flow rate
L*	object	Pipe length
D_unit	string	Output pipe diameter unit
u_unit	string	Output velocity unit
dP_unit	string	Output pressure drop unit
rho_unit	string	Output density unit

PIPEFLOWGASCalculate isothermal gas pipe flow: density, volumetric flow rate, mass flow rate from pressure drop

Calculate isothermal gas pipe flow: density, volumetric flow rate, mass flow rate from pressure drop

Parameter	Typ	Beschreibung
P1*	object	Upstream (inlet) pressure
P2*	object	Downstream (outlet) pressure
T*	object	Gas temperature
L*	object	Pipe length
D*	object	Pipe inside diameter
MW*	object	Gas molecular weight
rho_unit	string	Output density unit
Q_unit	string	Output volumetric flow unit (normal conditions)
M_unit	string	Output mass flow unit

PIPEFLOWLIQCalculate liquid pipe flow: volumetric flow rate and mass flow rate from pressure drop

Calculate liquid pipe flow: volumetric flow rate and mass flow rate from pressure drop

Parameter	Typ	Beschreibung
P1*	object	Upstream (inlet) pressure
P2*	object	Downstream (outlet) pressure
L*	object	Pipe length
D*	object	Pipe inside diameter
rho*	object	Liquid density
Q_unit	string	Output volumetric flow unit
M_unit	string	Output mass flow unit

CVGASCalculate gas control valve Cv and Kv from flow conditions

Calculate gas control valve Cv and Kv from flow conditions

Parameter	Typ	Beschreibung
Q*	object	Gas volumetric flow rate at standard conditions
P1*	object	Upstream pressure
P2*	object	Downstream pressure
T1*	object	Inlet gas temperature
MW*	object	Gas molecular weight
k*	object	Specific heat ratio (Cp/Cv)
Cv_unit	string	Output Cv unit
Kv_unit	string	Output Kv unit

CVLIQCalculate liquid control valve Cv and Kv from flow conditions

Calculate liquid control valve Cv and Kv from flow conditions

Parameter	Typ	Beschreibung
Q*	object	Liquid volumetric flow rate
P1*	object	Upstream pressure
P2*	object	Downstream pressure
rho*	object	Liquid density
Pv	object	Liquid vapor pressure (optional, default 0 kPa)
Pc	object	Liquid critical pressure (optional, default 22120 kPa)
FL	object	Liquid pressure recovery factor (optional, default 0.9)
Cv_unit	string	Output Cv unit
Kv_unit	string	Output Kv unit

CVSTEAMCalculate steam control valve Cv and Kv from flow conditions

Calculate steam control valve Cv and Kv from flow conditions

Parameter	Typ	Beschreibung
M*	object	Steam mass flow rate
P1*	object	Upstream pressure
P2*	object	Downstream pressure
rho*	object	Steam density
Cv_unit	string	Output Cv unit
Kv_unit	string	Output Kv unit

ORIFICEGASGas 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.

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.

Parameter	Typ	Beschreibung
M*	object	Gas mass flow rate. Set value='?' to calculate.
dP*	object	Differential pressure across orifice. Set value='?' to calculate.
D2*	object	Orifice bore diameter. Set value='?' to calculate.
P1*	object	Upstream (operating) pressure
D1*	object	Pipe inside diameter
rho*	object	Fluid density
mu*	object	Dynamic viscosity
k	object	Heat capacity ratio (Cp/Cv), default 1.4

ORIFICELIQLiquid 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.

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.

Parameter	Typ	Beschreibung
M*	object	Liquid mass flow rate. Set value='?' to calculate.
dP*	object	Differential pressure across orifice. Set value='?' to calculate.
D2*	object	Orifice bore diameter. Set value='?' to calculate.
P1*	object	Upstream (operating) pressure
D1*	object	Pipe inside diameter
rho*	object	Fluid density
mu*	object	Dynamic viscosity

VENTURIGASGas 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.

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.

Parameter	Typ	Beschreibung
M*	object	Gas mass flow rate. Set value='?' to calculate.
dP*	object	Differential pressure across Venturi meter. Set value='?' to calculate.
D2*	object	Venturi throat diameter. Set value='?' to calculate.
P1*	object	Upstream (operating) pressure
D1*	object	Pipe inside diameter
rho*	object	Fluid density
mu*	object	Dynamic viscosity
k	object	Heat capacity ratio (Cp/Cv), default 1.4

VENTURILIQLiquid 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.

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.

Parameter	Typ	Beschreibung
M*	object	Liquid mass flow rate. Set value='?' to calculate.
dP*	object	Differential pressure across Venturi meter. Set value='?' to calculate.
D2*	object	Venturi throat diameter. Set value='?' to calculate.
P1*	object	Upstream (operating) pressure
D1*	object	Pipe inside diameter
rho*	object	Fluid density
mu*	object	Dynamic viscosity

PSVGASCalculate required PSV (pressure safety valve) relief area for gas/vapor service per API 520

Calculate required PSV (pressure safety valve) relief area for gas/vapor service per API 520

Parameter	Typ	Beschreibung
M*	object	Relieving mass flow rate
P1*	object	Upstream relieving pressure (set pressure + overpressure + atm)
P2*	object	Downstream (back) pressure
T1*	object	Relieving temperature
MW*	object	Gas/vapor molecular weight
k	object	Heat capacity ratio (Cp/Cv), default 1.4
Kb	object	Capacity correction factor for back pressure, default 1.0
Kc	object	Combination correction factor (rupture disk), default 1.0
Kd	object	Effective coefficient of discharge, default 0.975
A_unit	string	Output relief area unit

PSVSTEAMCalculate required PSV (pressure safety valve) relief area for steam service per API 520

Calculate required PSV (pressure safety valve) relief area for steam service per API 520

Parameter	Typ	Beschreibung
M*	object	Relieving mass flow rate
P1*	object	Upstream relieving pressure (set pressure + overpressure + atm)
T1*	object	Relieving temperature
Kb	object	Capacity correction factor for back pressure, default 1.0
Kc	object	Combination correction factor (rupture disk), default 1.0
Kd	object	Effective coefficient of discharge, default 0.975
A_unit	string	Output relief area unit

PSVLIQCalculate required PSV (pressure safety valve) relief area for liquid service per API 520

Calculate required PSV (pressure safety valve) relief area for liquid service per API 520

Parameter	Typ	Beschreibung
M*	object	Relieving mass flow rate
P1*	object	Upstream relieving pressure (set pressure + overpressure + atm)
P2*	object	Downstream (back) pressure
Pover	object	Overpressure fraction (e.g. 0.1 = 10%), default 0.1
rho*	object	Liquid density
Kc	object	Combination correction factor (rupture disk), default 1.0
Kd	object	Effective coefficient of discharge, default 0.65
Kv	object	Viscosity correction factor, default 1.0
Kw	object	Back pressure correction factor (balanced bellows), default 1.0
A_unit	string	Output relief area unit

PUMPBHPCalculate pump brake horsepower

Calculate pump brake horsepower

Parameter	Typ	Beschreibung
rho*	object	Fluid density
Q*	object	Volumetric flow rate
P1*	object	Inlet pressure
P2*	object	Outlet pressure
Eff*	object	Pump efficiency
BHP_unit	string	Output power unit

COMPPOLYEFFCalculate polytropic efficiency of compressor

Calculate polytropic efficiency of compressor

Parameter	Typ	Beschreibung
Pi*	object	Inlet pressure
Po*	object	Outlet pressure
Ti*	object	Inlet temperature
To*	object	Outlet temperature
k*	object	Heat capacity ratio

TBNEFFCalculate steam turbine isentropic efficiency

Calculate steam turbine isentropic efficiency

Parameter	Typ	Beschreibung
Pi*	object	Inlet pressure
Ti*	object	Inlet temperature
Po*	object	Outlet pressure
To*	object	Actual outlet temperature
Eff_unit	string	Output efficiency unit

STGEFFCalculate multistage steam turbine isentropic efficiency

Calculate multistage steam turbine isentropic efficiency

Parameter	Typ	Beschreibung
M1*	object	Main steam flow
M2	object	Extraction steam flow #1
M3	object	Extraction steam flow #2
M4	object	Extraction steam flow #3
M5	object	Extraction steam flow #4
P1*	object	Stage pressure #1
T1*	object	Stage temperature #1
P2*	object	Stage pressure #2
T2*	object	Stage temperature #2
P3	object	Stage pressure #3
T3	object	Stage temperature #3
P4	object	Stage pressure #4
T4	object	Stage temperature #4
P5	object	Stage pressure #5
T5	object	Stage temperature #5
E*	object	Actual generator output
Eff_unit	string	—

HTRINOUTEFFCalculate fired heater heat duty and efficiency from inlet/outlet conditions and composition

Calculate fired heater heat duty and efficiency from inlet/outlet conditions and composition

Parameter	Typ	Beschreibung
HC*	object	Fuel gas hydrocarbon component list (e.g. ['CH4','C2H6'])
mole*	object	Fuel gas mole fraction list matching HC order (e.g. [0.9, 0.1])
Mfuel*	object	Fuel mass flow rate
Tfuel*	object	Fuel temperature
Tair*	object	Combustion air temperature
exO2*	object	Excess oxygen in flue gas
Trad*	object	Radiant section outlet temperature
Tstk*	object	Stack gas temperature
Mair_unit	string	Output air mass flow rate unit
MWfuel_unit	string	Output fuel molecular weight unit
LHVfuel_unit	string	Output fuel LHV unit
Qduty_unit	string	Output total heat duty unit
Qrad_unit	string	Output radiant section duty unit
Qconv_unit	string	Output convection section duty unit
Qloss_unit	string	Output heat loss unit

HTRLOSSEFFCalculate fired heater loss efficiency from ambient temperature, stack gas temperature and excess oxygen

Calculate fired heater loss efficiency from ambient temperature, stack gas temperature and excess oxygen

Parameter	Typ	Beschreibung
Type*	object	Fuel type
Tg*	object	Stack gas temperature
Ta*	object	Ambient temperature
exO2*	object	Excess oxygen

HEXRFHeat exchanger fouling resistance back-calculation from shell/tube-side operating conditions.

Heat exchanger fouling resistance back-calculation from shell/tube-side operating conditions.

Parameter	Typ	Beschreibung
Unknown*	string	Which unknown is being solved for.
D_shll*	object	Shell inside diameter
D_tube*	object	Tube outside diameter
D_wall*	object	Tube wall thickness
P_tube*	object	Tube pitch
S_baffle*	object	Baffle spacing
N_tube*	object	Number of tubes
L_tube*	object	Tube length
N_shllseri*	object	Number of shells in series
N_shllpara*	object	Number of shells in parallel
N_shllpass*	object	Number of shell-side passes
N_tubepass*	object	Number of tube-side passes
A_hex*	object	Total heat transfer area
R_shll*	object	Shell-side fouling resistance
R_tube*	object	Tube-side fouling resistance
F*	object	Correction factor (dimensionless)
k_hex*	object	Tube wall thermal conductivity
T_shll*	object	Shell-side temperature range [T1, T2] used for property evaluation
rho_shll*	object	Shell-side fluid density list
Cp_shll*	object	Shell-side fluid heat capacity list
mu_shll*	object	Shell-side fluid viscosity list
k_shll*	object	Shell-side fluid thermal conductivity list
T_tube*	object	Tube-side temperature range [T1, T2] used for property evaluation
rho_tube*	object	Tube-side fluid density list

LMTDCalculate LMTD of heat exchanger

Calculate LMTD of heat exchanger

Parameter	Typ	Beschreibung
Thi*	object	Hot inlet temperature
Tho*	object	Hot outlet temperature
Tci*	object	Cold inlet temperature
Tco*	object	Cold outlet temperature
LMTD_unit	string	Output LMTD unit

STEAMFLASHCalculate flash steam flow from pressure reduction

Calculate flash steam flow from pressure reduction

Parameter	Typ	Beschreibung
Mc*	object	Condensate flow rate
Pc*	object	Condensate pressure
Ps*	object	Steam header pressure
Ms_unit	string	Output flash steam flow unit

DESUPERHEATERCalculate 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.

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.

Parameter	Typ	Beschreibung
Min*	object	Inlet steam flow rate
Pin*	object	Inlet steam pressure
Tin*	object	Inlet steam temperature
Pout*	object	Outlet steam pressure
Tout*	object	Outlet steam temperature
Pbfw*	object	BFW (boiler feed water) pressure
Tbfw*	object	BFW (boiler feed water) temperature
Mbfw_unit	string	Required BFW (boiler feed water) flow unit
Mout_unit	string	Total output steam flow unit

HPADEPRESSCalculate depressurization gas volume and hold time for high pressure air storage vessel

Calculate depressurization gas volume and hold time for high pressure air storage vessel

Parameter	Typ	Beschreibung
V1*	object	Vessel volume
P1*	object	Initial pressure
P2*	object	Final pressure
Q2*	object	Gas consumption rate
V2_unit	string	Available gas volume unit
H_unit	string	Required hold time unit

GN2DEPRESSCalculate depressurization gas volume and hold time for gaseous nitrogen storage vessel

Calculate depressurization gas volume and hold time for gaseous nitrogen storage vessel

Parameter	Typ	Beschreibung
V1*	object	Vessel volume
P1*	object	Initial pressure
P2*	object	Final pressure
Q2*	object	Nitrogen consumption rate
V2_unit	string	Available gas volume unit
H_unit	string	Required hold time unit

LN2DEPRESSCalculate depressurization gas volumn abd hold time and saturation temperature for liquid nitrogen storage vessel

Calculate depressurization gas volumn abd hold time and saturation temperature for liquid nitrogen storage vessel

Parameter	Typ	Beschreibung
V1*	object	Tank volume
P1*	object	Initial pressure
P2*	object	Final pressure
Q2*	object	Nitrogen consumption rate
T1_unit	string	Required temperature unit
V2_unit	string	Available gas volume unit
H_unit	string	Required hold time unit

STMDEPRESSCalculate depressurization steam volumn and hold time for steam accumulator

Calculate depressurization steam volumn and hold time for steam accumulator

Parameter	Typ	Beschreibung
V1*	object	Accumulator volume
P1*	object	Initial pressure
P2*	object	Final pressure
M2*	object	Steam consumption rate
V2_unit	string	Available steam amount unit
H_unit	string	Required hold time unit

CTWREVAPORCooling tower evaporation rate: mass removal rate (MR) and heat removal rate (QR)

Cooling tower evaporation rate: mass removal rate (MR) and heat removal rate (QR)

Parameter	Typ	Beschreibung
INPUT*	object	—
OUTPUT	object	—

CTWRLGCooling tower L/G ratio calculation

Cooling tower L/G ratio calculation

Parameter	Typ	Beschreibung
INPUT*	object	—
OUTPUT	object	—

CTWRNTUCooling tower NTU and characteristic C value calculation

Cooling tower NTU and characteristic C value calculation

Parameter	Typ	Beschreibung
INPUT*	object	—
OUTPUT	object	—

CTWRCAPACooling tower capacity evaluation

Cooling tower capacity evaluation

Parameter	Typ	Beschreibung
INPUT*	object	—
OUTPUT	object	—

CTWRCAPADSNTSTCooling tower capacity evaluation: design vs test

Cooling tower capacity evaluation: design vs test

Parameter	Typ	Beschreibung
INPUT*	object	—
OUTPUT	object	—

DVRData Validation and Reconciliation

Data Validation and Reconciliation

Parameter	Typ	Beschreibung
MEASURED*	object	Measured values. Format: {TAG: {value: number, unit: string}}. Example: {A: {value: 100, unit: ''}}
ACCURACY*	object	Measurement accuracy in %. Format: {TAG: {value: number, unit: '%'}}. Example: {A: {value: 5, unit: '%'}}
EQUATION*	object	Constraint equations. Format: {EQ1: 'A=B+C', EQ2: 'C=D+E'}. Each value is an equation string with '=' separator.

advDVRAdvanced Data Validation and Reconciliation including gross error detection and elimation

Advanced Data Validation and Reconciliation including gross error detection and elimation

Parameter	Typ	Beschreibung
MEASURED*	object	Measured values. Format: {TAG: {value: number, unit: string}}. Example: {A: {value: 100, unit: ''}}
ACCURACY*	object	Measurement accuracy in %. Format: {TAG: {value: number, unit: '%'}}. Example: {A: {value: 5, unit: '%'}}
EQUATION*	object	Constraint equations. Format: {EQ1: 'A=B+C', EQ2: 'C=D+E'}. Each value is an equation string with '=' separator.

BALANCEGeneral mass/energy balance solver using GEKKO

General mass/energy balance solver using GEKKO

Parameter	Typ	Beschreibung
VARIABLE*	object	Decision variables. Each entry: [lb, init, ub] for free variable, or [fixed, fixed, fixed] for constant.
EQUATION*	object	Equality/inequality constraints. Keys prefixed eq/ge/le/gt/lt. Each entry: {'left': expr, 'right': expr}.
MINIMIZE	object	Objective to minimize. Format: {'left': 'mintarget', 'right': 'expr'}.
MAXIMIZE	object	Objective to maximize. Format: {'left': 'maxtarget', 'right': 'expr'}.

FORMULAGeneric formula calculator with unit conversion and IF-THEN-ELSE

Generic formula calculator with unit conversion and IF-THEN-ELSE

Parameter	Typ	Beschreibung
INPUT*	object	—
UNIT	object	—
FORMULA*	object	—
OUTPUT*	object	—

SOLVESolve nonlinear equations with unknown variables using fsolve

Solve nonlinear equations with unknown variables using fsolve

Parameter	Typ	Beschreibung
INPUT*	object	—
FORMULA*	object	—
OUTPUT*	object	—

ECONOMICEconomic analysis: NPV, IRR, Simple Payback, Profitability Index, EAC

Economic analysis: NPV, IRR, Simple Payback, Profitability Index, EAC

Parameter	Typ	Beschreibung
R	object	Discount rate (fraction, e.g. 0.1 for 10%). Default 0.1.
CF*	object	Cash flow list, period 0 (initial investment, negative) through final period, e.g. [-100000, 30000, 30000, 30000]

advECONOMICAdvanced Economic analysis with inflation, depreciation, and tax: NPV, IRR, Simple Payback, Profitability Index, NCF

Advanced Economic analysis with inflation, depreciation, and tax: NPV, IRR, Simple Payback, Profitability Index, NCF

Parameter	Typ	Beschreibung
INPUT*	object	—

58 von 58 Tools haben eine Beschreibung veröffentlicht.

Tool-Namen und -Beschreibungen stammen vom Publisher und werden wortgetreu als inerter Text angezeigt. Es sind die Zeichenketten, die ein MCP-Client an ein Modell übergibt, deshalb prüft Forge sie auf Prompt-Injection-Muster — jeder Befund erscheint oben beim Sicherheits-Scan. „Privilegiert“ ist ein Schlagwort-Treffer im Tool-Namen, keine Prüfung dessen, was das Tool tut: ein harmlos klingender Name kann trotzdem alles tun.

Über

Engineering calculation MCP server for oil and gas engineering applications.

Schlagwörter

mcp

Alternativen

Tool-Oberflächen werden verglichen…

com.engscript/mcp

Tools

Offengelegte Tools

Keine Abdeckung der Abhängigkeiten