Vapor-Liquid Equilibrium Engine

Vapor-Liquid Equilibrium Engine MCP Connector for Claude

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Calculate bubble points, dew points, and phase equilibrium properties for chemical mixtures.

4 tools Official Updated Oct 1, 2026 Official Vinkius Partner

This MCP server provides specialized thermodynamic tools for chemical process engineering. It allows AI agents to calculate critical phase equilibrium properties such as bubble points and dew points using various thermodynamic models. Users can determine equilibrium compositions and K-values for complex mixtures, and check for the existence of azeotropes. The engine supports ideal models, activity models, and Equations of State (EOS) to handle both ideal and non-ideal chemical behaviors.

vlethermodynamicschemical-engineeringphase-equilibriumazeotrope

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

calculate_bubble_point

Determines the conditions required for the first bubble of vapor to form from a liquid mixture

calculate_dew_point

Determines the conditions required for the first drop of liquid to form from a vapor mixture

get_equilibrium_properties

Calculates K-values and phase compositions at a fixed temperature and pressure

check_azeotrope_existence

Identifies if a mixture of specific components can form an azeotrope under specific conditions

See how to talk to your AI agent using Vapor-Liquid Equilibrium Engine.

What is the bubble point of a mixture of Benzene and Toluene at 1 atm using an ideal model? Composition: Benzene 0.4, Toluene 0.6

The bubble point temperature for the Benzene-Toluene mixture at 1 atm is 85.4°C.

Check if Ethanol and Water can form an azeotrope using an activity model.

Yes, Ethanol and Water can form an azeotrope.

Calculate the equilibrium properties for a mixture of Methanol and Acetone at 350K and 2 atm using the eos model. Composition: Methanol 0.5, Acetone 0.5

At 350K and 2 atm, the K-values are Methanol: 1.25 and Acetone: 0.85. The system is in the two-phase region.

The engine supports Ideal models, Activity models (like NRTL), and Equations of State (EOS) for non-ideal behavior.

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