MCP For Claude Marketplace
Ammonia Plant Design Suite

Ammonia Plant Design Suite MCP Connector for Claude

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Design ammonia synthesis plants using Haber-Bosch process modeling.

4 tools Official Updated Oct 1, 2026 Official Vinkius Partner
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This MCP server provides a complete suite of engineering tools for designing ammonia synthesis plants. It models the Haber-Bosch process by calculating critical parameters such as reformer sizing, synthesis loop pressure, and catalyst requirements. Engineers can use get_reformer_specs to determine unit dimensions, calculate_synthesis_loop for operational pressure, estimate_catalyst_requirements for material volume, and calculate_energy_and_integration to evaluate heat recovery and carbon footprint.

ammoniahaber-boschchemical-engineeringprocess-designindustrial

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

get_reformer_specs

Determines the required size and configuration of the steam reforming unit

calculate_energy_and_integration

Estimates total energy needs and the impact of heat recovery

calculate_synthesis_loop

Calculates the operational pressure and loop requirements for the ammonia synthesis stage

estimate_catalyst_requirements

Determines the volume of catalyst needed to meet production targets

See how to talk to your AI agent using Ammonia Plant Design Suite.

What are the specifications for a reformer using natural gas with an annual capacity of 500,000 metric tons?

The required reformer volume is 1250 cubic meters with a steam-to-carbon ratio of 3.0 and an operating temperature of 850 degrees Celsius.

Calculate the synthesis loop pressure for a plant producing 1,000,000 tons of ammonia per year using natural gas.

The required loop pressure is 250 bars with a recycle ratio of 4.5 and a total loop flow rate of 15,000 kg/s.

How much catalyst is needed for a loop pressure of 200 bars and an annual capacity of 200,000 tons?

The required catalyst volume is 450 cubic meters and the total catalyst mass is 320 metric tons.

The tools support natural gas and naphtha as primary hydrocarbon feedstocks for the reforming process.

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