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Ester Series

MMA (methyl methacrylate)

There are two prevailing processes for MMA, or methyl methacrylate production, C-2 Process starting from ethylene, methanol and formaldehyde, C-3 Process (also called as ACH Process) which uses the byproduct of HCN from acrylonitrile production as the feedstock, and C-4 process which uses isobutene or tertiary butanol as the feedstock. SL-TECH provides MMA plant based on C-4 Process, consisting of three working units, i.e. oxidation unit, distillation unit and esterification unit.

Introduction

There are two prevailing processes for MMA, or methyl methacrylate production, C-2 Process starting from ethylene, methanol and formaldehyde, C-3 Process (also called as ACH Process) which uses the byproduct of HCN from acrylonitrile production as the feedstock, and C-4 process which uses isobutene or tertiary butanol as the feedstock. SL-TECH provides MMA plant based on C-4 Process, consisting of three working units, i.e. oxidation unit, distillation unit and esterification unit.
Technical Features
The comparison of different process is reported as below. Though each process has its own advantages, when the plant capacity is lower than 100,000 TPA, C-4 Process is the most economic and therefore more recommended.
MMA Process Comparison
C-2 Process C-3 Process C-4 Process
Feed The ethylene, methanol, and formaldehyde can be used as the feed. It is required to use the byproduct of HCN from acrylonitrile unit as the feed. Isobutene or tertiary butynol (TBA) as the feed, which is easy to access.
Investment Cost High High Comparatively Low
Environmental Impact & Safety Performance Environmentally-friendly The treatment cost of the ammonium bisulfate-contained sewage is pretty high and is harmful to the environment. Environmentally-friendly
 
The MMA plant offered by SL-TECH has advantages such as easy availability of feedstock, more environment friendliness, lower investment, lower production cost and etc.
MMA specification
S/N Item Index
1 Purity, wt% ≥ 99.9
2 Color, APHA ≤ 10
3 Water Content, wt% ≤ 0.05
4 Acidity, wt% ≤ 0.005
5 Polymerization inhibitor, ppm 10

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