ccpp-tools-mcp
Server Configuration
Describes the environment variables required to run the server.
| Name | Required | Description | Default |
|---|---|---|---|
No arguments | |||
Instructions
Guidance the server publishes about itself, which clients place ahead of the tool catalog so the model reads it before choosing anything.
This server publishes no instructions, or was last inspected before Glama recorded them.
Capabilities
Features and capabilities supported by this server
Protocol revision2025-11-25
| Capability | Details |
|---|---|
| tools | {
"listChanged": false
} |
| prompts | {
"listChanged": false
} |
| resources | {
"subscribe": false,
"listChanged": false
} |
| experimental | {} |
Tools
Functions exposed to the LLM to take actions
| Name | Description |
|---|---|
| fluid_props_liquidA | Petroleum-liquid density/viscosity/vapor pressure at a temperature. Uses a named preset (currently 'diesel_no2', a representative ASTM D975 sample) or a custom fluid via api_gravity + two viscosity points [[T_degC, cSt], [T_degC, cSt]] (ASTM D341 fit) + vapor_pressure_kpa. |
| fluid_props_steamA | Water/steam properties (own IAPWS-IF97 implementation). Give both pressure and temperature for a single-phase state; only one of them for saturation properties at that pressure or temperature. |
| tank_capacityC | Storage-tank working/nominal volume and residence time from autonomy. |
| pipe_size_selectC | Select the smallest ASME B36.10M pipe meeting a velocity limit. |
| pipe_wall_thicknessC | ASME B31.1 pressure-design wall check against a selected schedule. |
| dp_segment_liquidB | Darcy-Weisbach + Crane K pressure drop for one liquid pipe segment. |
| list_crane_fittingsA | List fitting keys accepted by dp_segment_liquid and their K basis. |
| pump_tdhC | Pump total dynamic head from static lift, line losses, and pressures. |
| pump_npshaC | NPSH available at the pump; margin check when NPSHr is supplied. |
| pump_powerB | Hydraulic power, and shaft power when an efficiency is supplied. |
| valve_cv_liquidA | ISA 75.01 required Cv/Kv for turbulent liquid flow (Fp = 1). Supply inlet/vapor/critical pressures to enable the choked-flow check (for water use critical_pressure_bar_a = 220.64). |
Prompts
Interactive templates invoked by user choice
| Name | Description |
|---|---|
No prompts | |
Resources
Contextual data attached and managed by the client
| Name | Description |
|---|---|
No resources | |
TDQS
Scored across 11 tools
Each tool targets a distinct calculation or resource: fluid properties (liquid vs steam), tank sizing, pipe sizing/wall thickness/pressure drop, pump TDH/NPSHA/power, and valve Cv. No two tools overlap in purpose; even fluid_props_liquid and fluid_props_steam cover different fluids.
Tool names mostly follow a consistent object_attribute pattern (e.g., fluid_props_liquid, pipe_wall_thickness, pump_tdh). The one deviation is list_crane_fittings, which starts with a verb rather than a noun, but it is still clear and matches the underscore-separated lowercase style.
With 11 tools, the set is well-scoped for a chemical/process engineering domain. Each tool covers a distinct design step, and the count is within the ideal 3-15 range without feeling sparse or bloated.
The toolset covers a complete liquid piping and pump design workflow: fluid properties, tank capacity, pipe sizing, wall thickness, pressure drop, pump head/NPSH/power, and valve Cv. Minor gaps exist for gas/compressible flow calculations, but the domain appears intentionally liquid-focused.