MMA Plant
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There are three 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 TEC provides MMA plant based C-4 Process, consisting of three working units, i.e. oxidation unit, distillation unit and esterification unit.
Technical Features:
The MMA plant offered by SL TEC has advantages such as easy availability of feedstock, more environment friendliness, lower investment, lower production cost and etc.
1. Product Specification
S/N
|
Item
|
Index
|
1
|
Purity, wt%
|
≥99.9
|
2
|
Colour, APHA
|
≤10
|
3
|
Water Content, wt%
|
≤0.05
|
4
|
Acidity, wt%
|
≤0.005
|
5
|
Polymerization
Inhibitor, ppm |
10
|
S/N
|
Item
|
Consumption Rate
|
1
|
Tertiary Butanol (TBA), mt/mt of MMA
|
14.2
|
2
|
Methanol, mt/mt of MMA
|
3.35
|
3
|
Polymerization Inhibitor, kg/mt of MMA
|
30
|
4
|
De-foaming Agent, kg/mt of MMA
|
5
|
5
|
Extraction Solvent, kg/mt of MMA
|
32
|
6
|
Steam (3.6MPaG, 350oC) , mt/mt of MMA
|
19.2
|
7
|
Demineralized Water, mt/mt of MMA
|
2.56
|
8
|
Service Water, mt/mt of MMA
|
1.2
|
9
|
Cooling Water, mt/mt of MMA
|
5522
|
10
|
Low Temp. Water (5-10oC) , mt/mt of MMA
|
1869
|
11
|
Low Temp. Water (15-20oC) , mt/mt of MMA
|
73.6
|
12
|
Electricity, KWH/mt of MMA
|
3200
|
13
|
Instrument Air, Nm3/mt of MMA
|
472
|
14
|
Compressed Air, Nm3/mt of MMA
|
160
|
15
|
Nitrogen (0.5MPaG)
|
89.6
|

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