MCP For Claude Marketplace
Centrifugation Design Engineer

Centrifugation Design Engineer MCP Connector for Claude

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Design and size industrial centrifugation systems using Stokes' law and centrifugal physics.

4 tools Official Updated Oct 1, 2026 Official Vinkius Partner
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This MCP server provides specialized engineering tools for designing industrial centrifugation systems. It uses Stokes' law and centrifugal acceleration to calculate critical parameters for particle separation. Engineers can use get_separation_velocity to determine terminal settling speeds, calculate_required_g_force to find the necessary acceleration for specific timeframes, and size_centrifuge_system to estimate equipment capacity for both disc-stack and tubular architectures. Additionally, validate_separation_feasibility allows for quick verification of separation conditions based on fluid viscosity and density differences.

centrifugationstokes-lawfluid-dynamicsparticle-separationindustrial-engineering

4 tools expose this connector's capabilities to your AI agent.

calculate_required_g_force

Calculates the minimum centrifugal acceleration needed to achieve separation within a specific timeframe

get_separation_velocity

Determines the terminal settling velocity of a single particle within the fluid

size_centrifuge_system

Estimates the physical dimensions or capacity requirements for a centrifuge

validate_separation_feasibility

A quick check to see if a specific set of conditions will permit any separation at all

See how to talk to your AI agent using Centrifugation Design Engineer.

How fast will a 50-micrometer particle settle in a fluid with 0.001 Pa·s viscosity and a density difference of 500 kg/m^3 at 10,000 m/s^2?

The terminal settling velocity for the particle is 0.00025 m/s.

What G-force is needed to settle a 100-micrometer particle with a 200 kg/m^3 density delta in 10 seconds, given a viscosity of 0.002 Pa·s?

The required centrifugal acceleration is 15,625 m/s^2.

Estimate the size for a disc-stack centrifuge processing 5 m^3/h with a 20-micrometer particle and 100 kg/m^3 density difference (viscosity 0.001 Pa·s).

The required volume is 0.45 m^3 with an estimated residence time of 32.4 seconds using a disc-stack design.

The system supports design calculations for both disc-stack and tubular centrifuge architectures.

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