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Ethyl Acetate Dehydration Equipment

The manufacture of ethyl acetate traditionally relies on four primary production processes: esterification of acetic acid and ethyl ester, acetaldehyde condensation, catalytic dehydrogenation of ethanol, and adductive esterification of acetic acid and ethylene. However, the conventional process has faced challenges, including lower production technology standards, elevated costs, and subsequent supply-demand imbalances. These issues have led to reduced production, decreased profitability, and, in some cases, ceased production altogether.

Hence, the pursuit of a novel separation technology with low energy consumption, minimal environmental impact, and exceptional separation efficiency has emerged as a prominent trend in industrial production. Employing the pervaporation technique, ethyl acetate binary and ternary crude products can be efficiently separated using inorganic molecular sieve membranes, distinguished by their superior chemical stability and separation performance.

Made To Measure Solution

Additional information

Working Medium

Ethyl acetate, Methyl Acetate, Mixed Solvents

Material heating method

Steam

Production Material

Stainless Steel 304, Stainless Steel 316L

Product moisture content

0.01%~0.1%, 0.1%~0.2%, 0.2%~0.5%

Working Capacity

1000 TPA, 10000 TPA, 15000 TPA, 2000 TPA, 25000 TPA, 3000 TPA, 4000 TPA, 40000 TPA

Power (Input)

380V, 415V, 440V

Raw Material Moisture content

1%~30%

Description

A Process Technology For Dehydration and Recovery of Ethyl Acetate

Crude Binary Ternary Product Separation Of Ethyl Acetate Using Pervaporation Technique

The increasing demand for ethyl acetate as an important raw material in various industries demands the need for advanced production processes and effective recovery and dehydration technologies.

The traditional production processes, although widely used, face challenges such as high energy consumption, low separation efficiency, and environmental pollution.

The pervaporation technique has emerged as a promising alternative due to its low energy consumption, no pollution, and good separation effect.

Explore more details here.

 

Additional information

Working Medium

Ethyl acetate, Methyl Acetate, Mixed Solvents

Material heating method

Steam

Production Material

Stainless Steel 304, Stainless Steel 316L

Product moisture content

0.01%~0.1%, 0.1%~0.2%, 0.2%~0.5%

Working Capacity

1000 TPA, 10000 TPA, 15000 TPA, 2000 TPA, 25000 TPA, 3000 TPA, 4000 TPA, 40000 TPA

Power (Input)

380V, 415V, 440V

Raw Material Moisture content

1%~30%

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