Knowledge for the
Sulphuric Acid Industry 

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
Technology - CASOX
April 9, 2003
| Introduction | Associated Links | 
The CASOX Process is a SOx 
removal process using catalytic SOx-Oxidation using a newly developed high 
performance de-sulphurizing catalyst.  The CASOX Process leads to 
significant reductions in construction and operating costs, compared with 
conventional flue gas de-sulphurization processes such as lime scrubbing. 
Concentrated sulphuric acid, gypsum and ammonium sulphate can be produced as 
by-products of this process.
The process is easy to operate 
and maintain since the gas to be treated is simply passed though the catalyst 
bed.  The use of a monolith catalyst (i.e. honeycomb) enables the process 
to handle gases containing dust.
The CASOX Process adsorbs sulphur 
dioxide gas and oxidizes it with oxygen to form sulphur trioxide.  The 
presence of water vapour results in the formation of sulphuric acid which is 
removed and recovered.   The concentration of sulphuric acid is 
approximately 60%.  Since the acid formed is continuously removed, there is 
no requirement to regenerate the catalyst.
