Case Study — Polyethylene Plant

Olefin refining catalyst retrofit for a world-scale PE line

Retrofit of an olefin refining train removing AsH₃, PH₃, COS and O₂ from ethylene / 1-butene feed to a Ziegler-Natta polymerization unit.

Region · Middle East

Application background

The customer's world-scale polyethylene line was experiencing accelerated polymerization catalyst deactivation traced to trace arsine and carbonyl sulfide breakthrough from an aging olefin purification bed.

Feed gas & process conditions

GasEthylene + 1-butene comonomer feed
Flow60 t/h liquid ethylene, 8 t/h comonomer
Pressure4.0 MPa (g)
Temperature40 – 80 °C
Inlet impuritiesAsH₃ 20 ppb, PH₃ 10 ppb, COS 100 ppb, O₂ 500 ppb
Outlet requirementAll poisons < detection limit

Main impurity challenge

Simultaneous removal of arsine, phosphine, COS and oxygen from a hot olefin stream without olefin polymerization on the guard bed.

Recommended product

Olefin Purification Catalysts
Kaiteli OPC-As / OPC-DeOxy Guard-Bed Package

Multi-layer guard bed combining Cu/Ni-based deoxy, arsine absorbent and COS hydrolysis catalyst.

Technical result

  • All poisons reduced below detection at the polymerization inlet.
  • Ziegler-Natta polymerization catalyst life extended by > 40%.
  • Guard-bed change-out interval extended from 12 to 30 months.

Customer value

Recovered lost production capacity, reduced polymerization catalyst consumption and lowered off-spec polymer generation — payback in under 8 months.

Engineering Support

Need help selecting the right catalyst, adsorbent, or gas purifier?

Share your gas composition, impurity levels, flow rate, and outlet purity requirement. A Kaiteli process engineer will respond within one business day with a tailored selection and quotation.

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