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
Acid Regeneration
- Methyl Methacrylate (MMA) Spent Acid
February 25, 2002
Introduction Typical Composition |
Associated Links |
Methyl methacrylate is an intermediate used in the manufacture of acrylic resin, plastics, and paints. Most of the MMA produced in the world uses the acetone cyanohydrin (ACH) process which uses acetone as the feedstock. ICI (UK) produces approximately 85% of the world’s supply in plants located in the UK, USA and Taiwan.
The process uses concentrated sulphuric acid as part of the catalysis system and as a carrier in the reactor train. The MMA product is boiled of leaving an aqueous solution (spent acid) of ammonium sulphate, sulphuric acid and various organic compounds. Approximately 3 tonnes of spent acid is produced for every tonne of MMA produced.
The relatively low sulphuric acid concentration of the spent acid makes the spent acid difficult recover economically without employing additional technology and process steps. First the acid is preconcentrated which removes a larger portion of the water content. This has the effect of reducing fuel consumption, furnace size and downstream plant size. SO2 concentration is increased resulting in a smaller sulphuric acid plant contact section.
The degree of preconcentration is a function of the solubility of ammonium sulphate in solution. It is desirable to have the solution remain as a single phase.
Oxygen enrichment is also required to achieve satisfactory economics for the process. Varying degrees of oxygen enrichment can be done all the way to 100% oxygen.
Component | Formula | wt% |
Ammonium Sulphate | (NH4)2SO4 | 44.4 |
Sulphuric Acid | H2SO4 | 14.0 |
Water | H2O | 34.3 |
Ammonium Acetone Disulphonate | C3N2S2H12O7 | 2.0 |
Tars | as C14N2S2H35O14 | 3.3 |
Light Organics | as CH3OH | 0.4 |
Heavy Organics | as C4H6O | 1.4 |
Methacrylic Acid (Vinyl Acetate) | C4H6O2 | 0.4 |