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

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Knowledge for the Sulphuric Acid Industry
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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

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Acid Regeneration - Methyl Methacrylate (MMA) Spent Acid
February 25, 2002

Introduction
Typical Composition
Associated Links

Alkylation Spent Acid
Ammonium Sulphate Spent Acid


Introduction

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.

Typical Composition

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

 

 

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