com.engscript由 engscript.com 发布官方发布者v1.0.0更新于 Oct 24, 2026
Engineering calculation MCP server for oil and gas engineering applications.
让助手执行油气工程的热力学、流体与设备计算，例如混合物性质、管径、阀件与安全阀。
Web executable，通过 Streamable HTTP。 远程服务在工作区中配置后即可从网页运行时运行。
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"engscript-engineering": {
"type": "http",
"url": "https://engscript.com/mcp"
}
}
}Primary thermodynamic property calculator. Use this tool first for all mixture property calculations. Supports hydrocarbons and non-hydrocarbon chemicals (PR EOS flash calculation).
P必填T必填HC必填mole必填H_unitS_unitU_unitk_unitCp_unitCv_unitMW_unitmu_unit另有 3 个Calculate thermodynamic properties of hydrocarbon mixture. Supports hydrocarbons and non-hydrocarbon chemicals (PR EOS flash calculation).
P必填T必填HC必填mole必填H_unitS_unitCp_unitCv_unitrho_unitTbub_unitTdew_unitCalculate thermodynamic and transport properties of steam based on IAPWS
P必填T必填H_unitS_unitU_unitk_unitCp_unitCv_unitmu_unitrho_unitPsat_unitTsat_unitPsychrometric properties of moist air
BP必填DB必填DPRHWBH_unitV_unitDP_unitWB_unitrho_unitCalculate MW, LHV and HHV of fuel gas from composition
HC必填mole必填MW_unitHHV_unitLHV_unitCalculate enthalpy of flue gas from composition
HC必填Tb必填Tg必填mole必填Cp_unitMW_unitdH_unitCalculate CO2 emission conversion factor from gas composition
HC必填mole必填ECF_unitCalculate 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.
HPSTUrhoFluid必填C_unitH_unitL_unitM_unitO_unit另有 6 个Calculate gas molar volume using equation of state
P必填T必填V_unitConvert mass flow rate to volumetric flow rate at standard condition
M必填MW必填V_unitConvert volumetric flow rate to mass flow rate at standard condition and normal condition Sm3/hr, Nm3/hr, SCFH
V必填MW必填M_unitCalculate mean pressure between inlet and outlet
P1必填P2必填Fluid必填Pmean_unitCalculate Darcy friction factor based on Reynolds number and pipe roughness
D必填Re必填Piping必填Calculate steam leak mass flow and flow condition (CHOKED / SUBCRITICAL) based on upstream and downstream conditions
h必填CdP1必填P2必填T1必填T2必填M_unitCalculate mass flow from pin-hole on the steam piping
P必填T必填h必填CdM_unitCalculate 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.
Ta必填Tf必填ha必填NPS必填Tmax必填kins必填r2_unitr3_unittins_unitDpipe_unitQloss_unitTsurf_unitCalculate steam pipe sizing: pipe diameter, velocity, pressure drop
L必填M必填P必填T必填D_unitu_unitdP_unitrho_unitCalculate water pipe sizing: pipe diameter, velocity, pressure drop
L必填M必填P必填T必填D_unitu_unitdP_unitrho_unitCalculate compressed air pipe sizing: pipe diameter, velocity, pressure drop
L必填M必填P必填T必填D_unitu_unitdP_unitrho_unitCalculate nitrogen pipe sizing: pipe diameter, velocity, pressure drop
L必填M必填P必填T必填D_unitu_unitdP_unitrho_unitCalculate isothermal gas pipe flow: density, volumetric flow rate, mass flow rate from pressure drop
D必填L必填T必填MW必填P1必填P2必填M_unitQ_unitrho_unitCalculate liquid pipe flow: volumetric flow rate and mass flow rate from pressure drop
D必填L必填P1必填P2必填rho必填M_unitQ_unitCalculate gas control valve Cv and Kv from flow conditions
Q必填k必填MW必填P1必填P2必填T1必填Cv_unitKv_unitCalculate liquid control valve Cv and Kv from flow conditions
Q必填FLP1必填P2必填PcPvrho必填Cv_unitKv_unitCalculate steam control valve Cv and Kv from flow conditions
M必填P1必填P2必填rho必填Cv_unitKv_unitGas 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.
M必填kD1必填D2必填P1必填dP必填mu必填rho必填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.
M必填D1必填D2必填P1必填dP必填mu必填rho必填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.
M必填kD1必填D2必填P1必填dP必填mu必填rho必填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.
M必填D1必填D2必填P1必填dP必填mu必填rho必填Calculate required PSV (pressure safety valve) relief area for gas/vapor service per API 520
M必填kKbKcKdMW必填P1必填P2必填T1必填A_unitCalculate required PSV (pressure safety valve) relief area for steam service per API 520
M必填KbKcKdP1必填T1必填A_unitCalculate required PSV (pressure safety valve) relief area for liquid service per API 520
M必填KcKdKvKwP1必填P2必填rho必填PoverA_unitCalculate pump brake horsepower
Q必填P1必填P2必填Eff必填rho必填BHP_unitCalculate polytropic efficiency of compressor
k必填Pi必填Po必填Ti必填To必填Calculate steam turbine isentropic efficiency
Pi必填Po必填Ti必填To必填Eff_unitCalculate multistage steam turbine isentropic efficiency
E必填M1必填M2M3M4M5P1必填P2必填P3P4P5T1必填另有 5 个Calculate fired heater heat duty and efficiency from inlet/outlet conditions and composition
HC必填Tair必填Trad必填Tstk必填exO2必填mole必填Mfuel必填Tfuel必填Mair_unitQrad_unitQconv_unitQduty_unit另有 3 个Calculate fired heater loss efficiency from ambient temperature, stack gas temperature and excess oxygen
Ta必填Tg必填Type必填exO2必填Heat exchanger fouling resistance back-calculation from shell/tube-side operating conditions.
F必填A_hex必填k_hex必填D_shll必填D_tube必填D_wall必填L_tube必填N_tube必填P_tube必填Q_unitR_shll必填R_tube必填另有 29 个Calculate LMTD of heat exchanger
Tci必填Tco必填Thi必填Tho必填LMTD_unitCalculate flash steam flow from pressure reduction
Mc必填Pc必填Ps必填Ms_unitCalculate 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.
Min必填Pin必填Tin必填Pbfw必填Pout必填Tbfw必填Tout必填Mbfw_unitMout_unitCalculate depressurization gas volume and hold time for high pressure air storage vessel
P1必填P2必填Q2必填V1必填H_unitV2_unitCalculate depressurization gas volume and hold time for gaseous nitrogen storage vessel
P1必填P2必填Q2必填V1必填H_unitV2_unitCalculate depressurization gas volumn abd hold time and saturation temperature for liquid nitrogen storage vessel
P1必填P2必填Q2必填V1必填H_unitT1_unitV2_unitCalculate depressurization steam volumn and hold time for steam accumulator
M2必填P1必填P2必填V1必填H_unitV2_unitCooling tower evaporation rate: mass removal rate (MR) and heat removal rate (QR)
INPUT必填OUTPUTCooling tower L/G ratio calculation
INPUT必填OUTPUTCooling tower NTU and characteristic C value calculation
INPUT必填OUTPUTCooling tower capacity evaluation
INPUT必填OUTPUTCooling tower capacity evaluation: design vs test
INPUT必填OUTPUTData Validation and Reconciliation
ACCURACY必填EQUATION必填MEASURED必填Advanced Data Validation and Reconciliation including gross error detection and elimation
ACCURACY必填EQUATION必填MEASURED必填General mass/energy balance solver using GEKKO
EQUATION必填MAXIMIZEMINIMIZEVARIABLE必填Pinch analysis (minimum utilities, pinch temperatures, composite curves, grand composite curve) and heat exchanger network design by manual tick-off heuristic
INPUT必填OUTPUTPinch analysis (minimum utilities, pinch temperatures, composite curves, grand composite curve) and heat exchanger network design by optimization solver
INPUT必填OUTPUTGeneric formula calculator with unit conversion and IF-THEN-ELSE
UNITINPUT必填OUTPUT必填FORMULA必填Solve nonlinear equations with unknown variables using fsolve
INPUT必填OUTPUT必填FORMULA必填Economic analysis: NPV, IRR, Simple Payback, Profitability Index, EAC
RCF必填Advanced Economic analysis with inflation, depreciation, and tax: NPV, IRR, Simple Payback, Profitability Index, NCF
INPUT必填已满足适用检查项的 72%
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