Duae sunt processus praevalentes pro MMA seu productionis methacrylata methyl, C-2 Processus incipiens ab ethylene, methanolo et formaldehyde, C-3 Processus (etiam ACH Processus appellatus) qui utitur productione HCN ab acrylonitrili productione ut feeds, et C-4 processus qui utitur butanol isobutene vel tertiario sicut in feedstock. SL-TECH plantam MMA in C-4 processu praebet, tribus unitatibus laborantibus constans, i.e. oxidatio unitatis, distillationis unitatis et esterificationis unitatis.
| C-2 Process | C-3 Process | C-4 Process | |
| Feed | Ethylene, methanol et formaldehyde uti possunt pro pascuis. | Quaeritur uti productione HCN ex acrylonitrili unitatis ut in feed. | Isobutene vel tertiana butynol (TBA) quasi cibarium, quod aditu facile est. |
| Tractatus Pretium | Alta | Alta | Comparative Low |
| Environmental Impact & Safety Performance | Environmentally-amica | Curatio sumptus ammonium bisulfate contentum purgamentorum satis altum est et ambitus nocet. | Environmentally-amica |
| S/N | Res | Index |
| 1 | Puritas, wt% ≥ | 99.9 |
| 2 | Color, APHA ≤ | 10 |
| 3 | Aqua Content, wt% ≤ | 0.05 |
| 4 | Acidum, wt% ≤ | 0.005 |
| 5 | Polymerization inhibitor, ppm | 10 |
MIBK ( Methyl Isobuty Ketone ) Fabrica
Herba Chloroacetic Acid
Fabula Trioxane
Hydrogeni Peroxydum Fabrica
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