Ethylene Oxide (EO) and Vinyl Acetate Monomer (VAM) Production
Problem
In ethylene oxide (EO) production, oxygen and ethylene are reacted to form EO. Since the conversion per pass is not 100%, the reactor is operated in loop mode. Argon, which enters with the oxygen feed, builds up in the reactor loop and must be purged. The vinyl acetate monomer (VAM) process is very similar except acetic acid is also fed to the reactor. A portion of the ethylene feedstock is lost with the argon purge gas from the reactor loop. The value of the lost feedstock is substantial — approximately $500,000 per year for a typical EO or VAM plant.
VaporSep® Solution
Simplified EO or VAM production process showing addition of the VaporSep membrane system
The VaporSep system can achieve greater than 90% recovery of ethylene that would otherwise be flared. The VaporSep unit consists of a single-stage membrane system that separates ethylene vapors from argon. The ethylene-enriched permeate is sent to an existing compressor, then returned to the reactor; the argon-enriched residue is flared. VaporSep units are currently used by major EO producers including Samsung General Chemical and Formosa Plastics.
Benefits
VaporSep system for ethylene recovery
- Recovers valuable ethylene with payback time of 1 year or less
- Minimizes installation cost with skid-mounted construction
- Minimizes footprint and weight
- Operates at modest temperature and pressure
- Integrates into existing operations with minimal modifications
- Requires no additional rotating equipment
System Description
- Complete skid-mounted unit includes all necessary instrumentation and controls
- Typical size: 15 ft (L) x 6 ft (W) x 8 ft (H); 5000 lb
System Performance
- Typically 70% to 90% ethylene recovery
- Payback is 6 to 12 months