headerdrawing1.jpg (96365 bytes)

Sulphuric Acid on the WebTM Technical Manual DKL Engineering, Inc.

Knowledge for the Sulphuric Acid Industry Line.jpg (1139 bytes)

Sulphuric Acid on the Web

Introduction
General
Equipment Suppliers
Contractor

Instrumentation
Industry News
Maintenance
Acid Traders
Organizations
Fabricators
Conferences

Used Plants
Intellectual Propoerty
Acid Plant Database
Market Information
Library

Technical Manual

Introduction
General

Definitions
Instrumentation
Plant Safety
Metallurgial Processes
Metallurgical
Sulphur Burning
Acid Regeneration
Lead Chamber
Technology
Gas Cleaning
Contact
Strong Acid
Acid Storage
Loading/Unloading

Transportation
Sulphur Systems
Liquid SO2
Boiler Feed Water
Steam Systems

Cooling Water
Effluent Treatment
Utilities
Construction
Maintenance
Inspection
Analytical Procedures
Materials of Construction
Corrosion
Properties
Vendor Data

DKL Engineering, Inc.

Handbook of Sulphuric Acid Manufacturing
Order Form
Preface
Contents
Feedback

Sulphuric Acid Decolourization
Order Form
Preface
Table of Contents

Process Engineering Data Sheets - PEDS
Order Form
Table of Contents

Introduction

Bibliography of Sulphuric Acid Technology
Order Form

Preface
Contents

Sulphuric Acid Plant Specifications
 

Google Search new2.gif (111 bytes)

 

 


Technology - REGESOX™
February 15, 2003

Introduction
Associated Links

Introduction

The REGESOX™ process if used primarily for the treatment of gases containing low concentrations of CS2 / H2S.   These gases are typical of the viscose fibre production process.

Sulphuric acid in the concentration range of 40 to 60 wt%H2SO4 is produced as a by-product.

The REGESOX™ is a regenerative heat exchange process consisting of two reactors loaded with CS2 / H2S oxidation catalyst, SO2 conversion catalyst and inert heat exchange material.  Cold wet feed gas is heated by the treated gases leaving the second reactor.  The preheated gases enters the first reactor and is heated to the required reaction temperature by the inert heat exchange material.  The gases then pass through the CS2 / H2S oxidation catalyst followed by the SO2 conversion catalyst.  The oxidation reactions are exothermic and the temperature of the gas increases.  The hot gases pass from the first reactor into the second reactor where the hot gases are cooled while heating the catalyst and reactor material.  The remaining heat in the gas is used to preheat the incoming cold gas.

After 5-10 minutes, the flow is reversed.  The second reactor has sufficient heat stored in the inert heat exchange material to heat the cold incoming gases to the required reaction temperature.  The process of switching the first and second reactors is repeated.  The sulphuric acid that is formed will condense on the heat exchange material.

The acid is collected at a temperature of approximately 60°C and a concentration of approximately 50 wt% and may be recycled directly to the spinning plant acid system of the viscose fibre plant due to the high purity of the acid.

A fuel fired heater between both reactors compensates for any heat losses and is used mainly during start-up.  The system can thus be operated with nearly zero fuel consumption.