MCP For Claude Marketplace
Ethylene Glycol Plant Designer

Ethylene Glycol Plant Designer MCP Connector for Claude

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Chemical engineering tool for modeling ethylene glycol production and reactor design.

4 tools Official Updated Oct 1, 2026 Official Vinkius Partner
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This MCP server provides specialized chemical engineering tools to design and optimize ethylene glycol production plants. It allows users to calculate reactor specifications using calculate_reactor_design, estimate product yields with predict_product_distribution, determine distillation conditions via optimize_separation_parameters, and assess financial feasibility with evaluate_plant_economics. The tools model the hydration of ethylene oxide and the subsequent separation of MEG, DEG, and TEG.

chemical-engineeringethylene-glycolreactor-designprocess-optimizationindustrial-chemistry

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

evaluate_plant_economics

Assesses the feasibility of a design based on throughput and product mix

calculate_reactor_design

Determines the required reactor physical specifications based on feedstock and target output

optimize_separation_parameters

Provides the necessary operating conditions for the distillation train to achieve a specific product purity

predict_product_distribution

Estimates the yield of MEG, DEG, and TEG

See how to talk to your AI agent using Ethylene Glycol Plant Designer.

Calculate the reactor design for 500 units of EO with a water-to-EO ratio of 10 and a target capacity of 1000.

The required reactor volume is 1250 m³, with a residence time of 45 minutes and a heat duty of 450 MW.

What is the expected product distribution if the water-to-EO ratio is 15 and residence time is 60 minutes?

The expected yield is 85% MEG, 12% DEG, and 3% TEG.

Estimate the plant economics for a design with 1000 units of capacity and EO cost of 50 per unit.

The projected gross margin is $250,000 with an operating cost of $150,000 and revenue of $400,000.

You can use the `calculate_reactor_design` tool by providing the available ethylene oxide, the target plant capacity, and the desired water-to-EO ratio.

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