# MTBE/ETBE Production Design AI Agent Connect

> Design etherification units for MTBE and ETBE production using kinetic modeling and reactive distillation.

## Overview
- **Category:** engineering
- **Price:** Free
- **Endpoint:** https://edge.vinkius.com/vk_preview_DfCbd1f0zpjJvVZkauBmtiLIGtYVQy63xqNFJrjB/ai-agent-connect
- **Tags:** etherification, kinetics, reactor-design, catalyst, chemical-engineering

## Description

This MCP server provides specialized engineering tools for designing etherification units. It allows users to calculate reaction kinetics, size reactor vessels, estimate catalyst lifecycles, and evaluate feedstock viability for producing Methyl Tertiary Butyl Ether (MTBE) or Ethyl Tertiary Butyl Ether (ETBE). By utilizing `calculate_reaction_kinetics`, engineers can determine theoretical conversion limits. The `design_reactor_unit` tool facilitates sizing physical vessels, including support for reactive distillation to optimize yields. Additionally, `estimate_catalyst_lifecycle` helps predict maintenance needs, while `evaluate_feedstock_viability` ensures raw material availability meets production targets.

## Tools

### evaluate_feedstock_viability
Determine if the available raw materials can meet the desired ether production levels

### calculate_reaction_kinetics
Determine the theoretical reaction rate and conversion potential based on chemical feed composition and temperature

### design_reactor_unit
Size the physical reactor vessel required to achieve a specific production target

### estimate_catalyst_lifecycle
Predict how much catalyst is needed to sustain production over a specific timeframe

## Prompt Examples

**Prompt:** 
```
What is the theoretical conversion for methanol and isobutene at 50 degrees Celsius with a 1.1 alcohol ratio and 0.95 purity?
```

**Response:** 
```
The theoretical conversion is 0.88 with a reaction rate constant of 0.045 and an equilibrium constant of 12.4.
```

**Prompt:** 
```
I need to produce 500 kg/h of ether with 0.85 conversion. How big should my reactor be if I use reactive distillation?
```

**Response:** 
```
The required reactor volume is 12.5 m3, with a residence time of 45 minutes and a catalyst mass of 250 kg.
```

**Prompt:** 
```
Will 1000kg of methanol and 800kg of isobutene be enough for a 0.9 yield?
```

**Response:** 
```
No, the maximum possible yield is 0.82, which is below your required 0.9 yield.
```

## Frequently Asked Questions

**How do I calculate the required reactor size?**
You should first use `calculate_reaction_kinetics` to get the kinetic data, then pass that data into `design_reactor_unit` along with your target production rate.

**Can I design for reactive distillation?**
Yes, the `design_reactor_unit` tool includes a parameter to enable reactive distillation modeling, which can reduce the required reactor volume.

**How can I check if my feedstock is sufficient?**
Use the `evaluate_feedstock_viability` tool by providing the mass of available alcohol, available isobutene, and your required yield.