EngScript Engineering MCP
com.engscript/mcpVersion 1.0.0Engineering calculation MCP server for oil and gas engineering applications.
Status
Responds126 msAnswered our handshake without sign-in.- Last checked
- Nov 14, 2026, 13:55 UTC
- Latency
- 126 ms
- Remotes responding
- 1 of 1
- Sign-in
- No sign-in
- Hosting
- EU hosting detected (detected, not a legal statement)
- Registry data as of
- Nov 14, 2026, 21:12 UTC
Data from the official MCP Registry, checked by run.zero. How we check
Connect
Streamable HTTP
https://engscript.com/mcpResponds126 msNo sign-in
Claude Code
claude mcp add --transport http engscript https://engscript.com/mcpClaude Desktop and claude.ai
Settings > Connectors > Add custom connector
Name: engscript
Remote MCP server URL: https://engscript.com/mcpCursor
{
"mcpServers": {
"engscript": {
"url": "https://engscript.com/mcp"
}
}
}VS Code
code --add-mcp '{"name":"engscript","type":"http","url":"https://engscript.com/mcp"}'Built your own server? run.zero hosts MCP servers on European infrastructure.
Tools
60 tools
Read-only | Idempotent | Open world | ||
|---|---|---|---|---|
advDVRAdvanced Data Validation and Reconciliation including gross error detection and elimation | Not declared | Not declared | Not declared | Not declared |
advECONOMICAdvanced Economic analysis with inflation, depreciation, and tax: NPV, IRR, Simple Payback, Profitability Index, NCF | Not declared | Not declared | Not declared | Not declared |
BALANCEGeneral mass/energy balance solver using GEKKO | Not declared | Not declared | Not declared | Not declared |
CARBONCalculate thermodynamic properties of hydrocarbon mixture. Supports hydrocarbons and non-hydrocarbon chemicals (PR EOS flash calculation). | Not declared | Not declared | Not declared | Not declared |
COMPPOLYEFFCalculate polytropic efficiency of compressor | Not declared | Not declared | Not declared | Not declared |
CTWRCAPACooling tower capacity evaluation | Not declared | Not declared | Not declared | Not declared |
CTWRCAPADSNTSTCooling tower capacity evaluation: design vs test | Not declared | Not declared | Not declared | Not declared |
CTWREVAPORCooling tower evaporation rate: mass removal rate (MR) and heat removal rate (QR) | Not declared | Not declared | Not declared | Not declared |
CTWRLGCooling tower L/G ratio calculation | Not declared | Not declared | Not declared | Not declared |
CTWRNTUCooling tower NTU and characteristic C value calculation | Not declared | Not declared | Not declared | Not declared |
CVGASCalculate gas control valve Cv and Kv from flow conditions | Not declared | Not declared | Not declared | Not declared |
CVLIQCalculate liquid control valve Cv and Kv from flow conditions | Not declared | Not declared | Not declared | Not declared |
CVSTEAMCalculate steam control valve Cv and Kv from flow conditions | Not declared | Not declared | Not declared | Not declared |
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. | Not declared | Not declared | Not declared | Not declared |
DVRData Validation and Reconciliation | Not declared | Not declared | Not declared | Not declared |
ECONOMICEconomic analysis: NPV, IRR, Simple Payback, Profitability Index, EAC | Not declared | Not declared | Not declared | Not declared |
EMISSIONFACTORCalculate CO2 emission conversion factor from gas composition | Not declared | Not declared | Not declared | Not declared |
FLUEGASCalculate enthalpy of flue gas from composition | Not declared | Not declared | Not declared | Not declared |
FORMULAGeneric formula calculator with unit conversion and IF-THEN-ELSE | Not declared | Not declared | Not declared | Not declared |
FUELGASCalculate MW, LHV and HHV of fuel gas from composition | Not declared | Not declared | Not declared | Not declared |
GN2DEPRESSCalculate depressurization gas volume and hold time for gaseous nitrogen storage vessel | Not declared | Not declared | Not declared | Not declared |
HEXRFHeat exchanger fouling resistance back-calculation from shell/tube-side operating conditions using Kern + Dittus-Boelter. | Not declared | Not declared | Not declared | Not declared |
HEXRF_DGHeat exchanger fouling resistance back-calculation from shell/tube-side operating conditions using Delaware + Gnielinski. | Not declared | Not declared | Not declared | Not declared |
HEXRF_KDHeat exchanger fouling resistance back-calculation from shell/tube-side operating conditions using Kern + Dittus-Boelter. | Not declared | Not declared | Not declared | Not declared |
HPADEPRESSCalculate depressurization gas volume and hold time for high pressure air storage vessel | Not declared | Not declared | Not declared | Not declared |
HTRINOUTEFFCalculate fired heater heat duty and efficiency from inlet/outlet conditions and composition | Not declared | Not declared | Not declared | Not declared |
HTRLOSSEFFCalculate fired heater loss efficiency from ambient temperature, stack gas temperature and excess oxygen | Not declared | Not declared | Not declared | Not declared |
LMTDCalculate LMTD of heat exchanger | Not declared | Not declared | Not declared | Not declared |
LN2DEPRESSCalculate depressurization gas volumn abd hold time and saturation temperature for liquid nitrogen storage vessel | Not declared | Not declared | Not declared | Not declared |
MIXTUREPrimary thermodynamic property calculator. Use this tool first for all mixture property calculations. Supports hydrocarbons and non-hydrocarbon chemicals (PR EOS flash calculation). | Not declared | Not declared | Not declared | Not declared |
MtoVConvert mass flow rate to volumetric flow rate at standard condition | Not declared | Not declared | Not declared | Not declared |
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. | Not declared | Not declared | Not declared | Not declared |
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. | Not declared | Not declared | Not declared | Not declared |
PIPEAIRCalculate compressed air pipe sizing: pipe diameter, velocity, pressure drop | Not declared | Not declared | Not declared | Not declared |
PIPEFFCalculate Darcy friction factor based on Reynolds number and pipe roughness | Not declared | Not declared | Not declared | Not declared |
PIPEFLOWGASCalculate isothermal gas pipe flow: density, volumetric flow rate, mass flow rate from pressure drop | Not declared | Not declared | Not declared | Not declared |
PIPEFLOWLIQCalculate liquid pipe flow: volumetric flow rate and mass flow rate from pressure drop | Not declared | Not declared | Not declared | Not declared |
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. | Not declared | Not declared | Not declared | Not declared |
PIPENITROGENCalculate nitrogen pipe sizing: pipe diameter, velocity, pressure drop | Not declared | Not declared | Not declared | Not declared |
PIPESTEAMCalculate steam pipe sizing: pipe diameter, velocity, pressure drop | Not declared | Not declared | Not declared | Not declared |
PIPEWATERCalculate water pipe sizing: pipe diameter, velocity, pressure drop | Not declared | Not declared | Not declared | Not declared |
PmeanCalculate mean pressure between inlet and outlet | Not declared | Not declared | Not declared | Not declared |
PSVGASCalculate required PSV (pressure safety valve) relief area for gas/vapor service per API 520 | Not declared | Not declared | Not declared | Not declared |
PSVLIQCalculate required PSV (pressure safety valve) relief area for liquid service per API 520 | Not declared | Not declared | Not declared | Not declared |
PSVSTEAMCalculate required PSV (pressure safety valve) relief area for steam service per API 520 | Not declared | Not declared | Not declared | Not declared |
PSYCHROMETRICPsychrometric properties of moist air | Not declared | Not declared | Not declared | Not declared |
PTVCalculate gas molar volume using equation of state | Not declared | Not declared | Not declared | Not declared |
PUMPBHPCalculate pump brake horsepower | Not declared | Not declared | Not declared | Not declared |
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. | Not declared | Not declared | Not declared | Not declared |
SOLVESolve nonlinear equations with unknown variables using fsolve | Not declared | Not declared | Not declared | Not declared |
STEAMCalculate thermodynamic and transport properties of steam based on IAPWS | Not declared | Not declared | Not declared | Not declared |
STEAMFLASHCalculate flash steam flow from pressure reduction | Not declared | Not declared | Not declared | Not declared |
STEAMLEAKCalculate steam leak mass flow and flow condition (CHOKED / SUBCRITICAL) based on upstream and downstream conditions | Not declared | Not declared | Not declared | Not declared |
STEAMPHCalculate mass flow from pin-hole on the steam piping | Not declared | Not declared | Not declared | Not declared |
STGEFFCalculate multistage steam turbine isentropic efficiency | Not declared | Not declared | Not declared | Not declared |
STMDEPRESSCalculate depressurization steam volumn and hold time for steam accumulator | Not declared | Not declared | Not declared | Not declared |
TBNEFFCalculate steam turbine isentropic efficiency | Not declared | Not declared | Not declared | Not declared |
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. | Not declared | Not declared | Not declared | Not declared |
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. | Not declared | Not declared | Not declared | Not declared |
VtoMConvert volumetric flow rate to mass flow rate at standard condition and normal condition Sm3/hr, Nm3/hr, SCFH | Not declared | Not declared | Not declared | Not declared |
Details
- Registry status
- Active
- Published
- Aug 14, 2026
- Updated
- Aug 14, 2026
- Website
- Not given
- Repository
- Not given
- Categories
- Uncategorized
- GDPR
- Not declared