The UOP/HYDRO Methanol-to-Olefins (MTO) Process produces ethylene and propylene from methanol derived from raw materials such as natural gas, coal, petroleum coke or biomass. This…
Tag: Ethylene
To convert a wide range of hydrocarbon feedstocks, from ethane to vacuum gasoils (VGOs), into high-value light olefins. High olefins fluid catalytic cracking (HO FCC)…
Advanced steam-cracking and cryogenic recovery process to produce polymer-grade ethylene and propylene, butadiene-rich mixed C4s, aromatic-rich pyrolysis gasoline, hydrogen and fuel streams. Cracking feedstocks range…
Shaw’s Refinery Offgas (ROG) technology is used to purify fluid catalytic cracker (FCC) unit offgas. Normally, this contaminated gas is combined with the refinery fuel…
Upgrade natural gas condensate and other contaminated streams to higher-value ethylene plant feedstocks. Mercury, arsenic and lead contamination in potential ethylene plant feedstocks precludes their…
The MaxEne process increases the ethylene yield from naphtha crackers by raising the concentration of normal paraffins (nparaffins) in the naphtha-cracker feed. The MaxEne process…
To produce polymer-grade ethylene and propylene by thermally cracking hydrocarbon feedstocks (ethane through hydro-cracked residue). Shaw’s key process technologies are: 1. Ultra-selective cracking (USC) furnaces—Selective…
To produce polymer-grade ethylene and propylene, a butadiene rich C4 cut, an aromatic C6 – C8 rich-raw pyrolysis gasoline and high-purity hydrogen by using the…
Thermal cracking of a wide range of feedstocks into light olefins (mainly ethylene and propylene) and aromatics using proprietary cracking coils. Feedstocks: Ethane, propane through…
To produce polymer-grade ethylene and propylene, a butadiene rich C4 cut, an aromatic C6–C8 rich raw pyrolysis gasoline and a high-purity hydrogen by steam pyrolysis…