MCP For Claude Marketplace
Propylene Production Designer

Propylene Production Designer MCP Connector for Claude

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Engineering design tool for modeling on-purpose propylene production pathways.

4 tools Official Updated Oct 1, 2026 Official Vinkius Partner
More Details Connect to Claude

This MCP server provides specialized engineering tools to design propylene production facilities. It allows users to model different chemical pathways including Propane Dehydrogenation (PDH), Methanol to Olefins (MTO), and Metathesis. Use calculate_reactor_specs to determine physical vessel requirements, design_catalyst_system to specify catalyst mass and type, and estimate_propylene_yield to calculate output efficiency. You can also use validate_process_feasibility to audit if a specific feedstock and technology combination is chemically viable.

propylenechemical-engineeringpdhmtometathesis

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

design_catalyst_system

Specifies the necessary catalyst mass and type to support the production capacity

calculate_reactor_specs

Determines the physical requirements and operational parameters of the reactor based on the chosen technology

estimate_propylene_yield

Calculates the expected output efficiency of the plant

validate_process_feasibility

An audit tool to check if the combination of feedstock, technology, and capacity is chemically and economically viable

See how to talk to your AI agent using Propylene Production Designer.

Calculate the reactor specifications for a PDH plant with a capacity of 50000 metric tons using propane.

The reactor for your PDH plant requires a volume of 1250 m³, a thermal load of 450 MW, an operating temperature of 620°C, and a pressure of 1.5 bar.

What is the expected propylene yield for an MTO process with 10000 tons of methanol?

The expected propylene yield is 4200 metric tons, with a conversion rate of 42% and a byproduct profile primarily consisting of ethylene.

Is it feasible to use ethylene for a metathesis process with a capacity of 20000 tons?

Yes, the process is viable with a low risk level, provided the stoichiometric availability of the olefin feedstock is maintained.

The server supports Propane Dehydrogenation (PDH), Methanol to Olefins (MTO), and Metathesis pathways.

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