Technology Introduction:
There are 4 main prevailing processes for ethyl acetate production, i.e. Direct Esterification Process, Acetaldehyde Condensation Process, Ethanol Dehydration Process and Acetic Acid-Ethylene Addition Process. Each process has its advantages and its applicable services. Our process is based on reactive-distillation esterification, which is mature, low costing and suitable for those with acetic acid feedstock.
Technical Features:
Advantages of Our Ethyl Acetate Plant and Process Technology
In our reactive distillation process, organic acid catalyst is used; its advantages cover the followings:
• Low ethanol consumption
• Low catalyst dosage
• High catalysis activity
• Low equipment corrosion
• Less side reactions
• Higher product purity
• Simple post-treatment operations
Typical Product Specification
|
S/N
|
Item
|
Unit
|
Index
|
|
1
|
Purity*
|
% wt
|
≧99.5
|
|
2
|
Ethanol
|
% wt
|
≦0.20
|
|
3
|
Moisture
|
% wt
|
≦0.10
|
|
4
|
Acidity as per CH3COOH
|
% wt
|
≦0.005
|
|
5
|
Color
|
Pt-Co Unit
|
≦10
|
|
6
|
Density (20oC)
|
g/cm3
|
0.897-0.902
|
|
7
|
Evaporation Residue
|
% wt
|
≦0.005
|
|
8
|
Odour
|
/
|
meeting typical odor, smelly odor free, residue odor free
|
*A higher ethyl acetate purity over 99.7% can be achieved if needed. Pls contact us for details.
(Contact Us)
Performance
Unit Consumption
|
S/N
|
Item
|
Consumption Rate
|
|
1
|
95% vol Ethanol
(mt/ mt@ 99.5% ethyl acetate)
|
0.58
|
|
2
|
99.50% wt Acetic Acid
(mt/ mt@ 99.5% ethyl acetate)
|
0.695
|
|
3
|
Catalyst
( content by weight)
|
2.7% for the first load
|
|
4
|
Steam
(mt/ mt@ 99.5% ethyl acetate)
|
2.5
|
|
5
|
Electricity
(KWH/ mt@ 99.5% ethyl acetate)
|
30
|
|
6
|
Circulating Water
(mt/ mt@ 99.5% ethyl acetate)
|
120
|
Hubei Sanli Fengxiang Technology Co., Ltd
Basic Information
Business Type:
Main Products:Methyl Acetate Plant, Phenol Alkylation Technology, Phenol Purification Technology, Distillation Technology, MMA Plant, MEG Plant, Hydrogen Peroxide Plant
Location:
Total Employees:
Year Established:
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Overseas Office: No
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