# Sour Water Stripper Design Tool AI Agent Connect

> Design and size Sour Water Stripper (SWS) units for acid gas removal.

## Overview
- **Category:** engineering
- **Price:** Free
- **Endpoint:** https://edge.vinkius.com/vk_preview_NObVpJZN6BDGxyFloexNoW8xR1x4925rW1foqSJw/ai-agent-connect
- **Tags:** sour-water, stripping, h2s-removal, ammonia-removal, distillation

## Description

This MCP server provides specialized engineering tools for designing Sour Water Stripper (SWS) units. It allows users to calculate column dimensions, steam requirements, and effluent quality for both single-stage and high-efficiency two-stage configurations. Use `get_single_stage_design` for standard sizing, `get_two_stage_design` for high-efficiency requirements, or `compare_designs` to evaluate the trade-offs between CAPEX and OPEX. You can also use `validate_effluent_compliance` to ensure your stripped water meets environmental limits.

## Tools

### get_two_stage_design
Calculates the dimensions and requirements for a high-efficiency two-stage stripping configuration

### validate_effluent_compliance
Checks if a given stripped water quality meets the required environmental or process specifications

### get_single_stage_design
Calculates the dimensions and requirements for a standard single-stage stripping column

### compare_designs
Provides a side-by-side comparison of single-stage and two-stage configurations

## Prompt Examples

**Prompt:** 
```
Calculate a single-stage design for 100 m3/h of sour water with 50 ppm H2S and 100 ppm NH3, targeting 5 ppm H2S and 10 ppm NH3.
```

**Response:** 
```
The single-stage design requires a column diameter of 1.2 meters and a height of 15 meters, with a steam flow rate of 12.5 m3/h to achieve the target quality.
```

**Prompt:** 
```
Compare single-stage and two-stage designs for 50 m3/h water, 100 ppm H2S, 200 ppm NH3, targeting 2 ppm H2S and 5 ppm NH3.
```

**Response:** 
```
The two-stage design is recommended for this high-ammonia load as it provides significantly better steam efficiency despite the higher initial capital cost.
```

**Prompt:** 
```
Is a stripped water sample with 8 ppm H2S and 12 ppm NH3 compliant with limits of 10 ppm H2S and 15 ppm NH3?
```

**Response:** 
```
Yes, the water is compliant as both H2S and NH3 concentrations are below the specified limits.
```

## Frequently Asked Questions

**When should I use a two-stage design?**
A two-stage design is recommended when dealing with high ammonia concentrations or when extremely strict effluent limits must be met, as it optimizes steam consumption and separation efficiency.

**How do I check if my water meets environmental limits?**
You can use the `validate_effluent_compliance` tool by providing the actual H2S and NH3 concentrations alongside your target limits.

**What inputs are required for the design tools?**
The tools require the water flow rate, the concentration of H2S and NH3 in the feed, and the target effluent concentrations for both gases.